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State-of-the-Art Chamber Facility for Studying Atmospheric Aerosol ...

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time <strong>for</strong> diffusion to <strong>the</strong> wall <strong>of</strong> <strong>the</strong> present chamber is 1<br />

min. However, FEP Teflon film is nonabsorptive to most<br />

hydrocarbons; measured losses <strong>of</strong> C 6F 6 and m-xylene are<br />

0.001 h -1 (loss rate includes potential leaks).<br />

Acknowledgments<br />

This work was supported by <strong>the</strong> U.S. Environmental Protection<br />

Agency Center on Airborne Organics and U.S. Environmental<br />

Protection Agency Agreement CR827331-01-0.<br />

FIGURE 10. Illustration <strong>of</strong> different processes occurring within <strong>the</strong><br />

chamber. Pathways include <strong>the</strong> following: (1) condensation, (2)<br />

gas-phase wall adsorption, (3) gas-deposited particle transport, (4)<br />

particle-wall transport, and (5) coagulation.<br />

<strong>the</strong> number concentration. Because coagulation is a secondorder<br />

process, <strong>the</strong> rate <strong>of</strong> reduction in <strong>the</strong> number concentration<br />

by coagulation decreases much more rapidly than<br />

does particle loss to <strong>the</strong> walls.<br />

Table 2 gives characteristic times <strong>for</strong> chamber processes<br />

important in gas-to-particle conversion. Note that <strong>the</strong> only<br />

significant change in particle number concentration occurs<br />

through wall deposition processes (except when nucleation<br />

occurs). There<strong>for</strong>e, <strong>the</strong> number <strong>of</strong> particles in <strong>the</strong> chamber<br />

can be described by <strong>the</strong> first-order wall loss rate as N ) N oe -βt .<br />

As <strong>the</strong> mass transfer rate to suspended particles greatly<br />

exceeds that <strong>of</strong> those deposited on <strong>the</strong> wall, <strong>the</strong> amount <strong>of</strong><br />

organic material associated with each particle at <strong>the</strong> time <strong>of</strong><br />

deposition is assumed to be constant. Thus, <strong>the</strong> total organic<br />

material produced is estimated to be <strong>the</strong> sum <strong>of</strong> that still<br />

suspended in <strong>the</strong> aerosol phase plus that deposited to <strong>the</strong><br />

wall. The particle size increases due to condensation <strong>of</strong><br />

organic vapors (and any nucleation products). The final size<br />

<strong>of</strong> <strong>the</strong> particles less <strong>the</strong> initial size <strong>of</strong> <strong>the</strong> seed particles provides<br />

an estimate <strong>of</strong> <strong>the</strong> volume <strong>of</strong> organic material suspended in<br />

<strong>the</strong> chamber. Figure 10 illustrates <strong>the</strong> competing processes.<br />

Adsorption <strong>of</strong> gas-phase compounds on <strong>the</strong> wall might<br />

possibly decrease <strong>the</strong>ir concentrations since <strong>the</strong> characteristic<br />

Literature Cited<br />

(1) Carter, W. P. L.; Luo, D.; Malkina, I. L.; Pierce, J. A. Environmental<br />

chamber studies <strong>of</strong> atmospheric reactivities <strong>of</strong> volatile organic<br />

compounds. Effects <strong>of</strong> varying chamber and light source; Final<br />

report to National Renewable Energy Laboratory; 1995 (http://<br />

cert.ucr.edu/∼carter/absts.htm#explrept).<br />

(2) Liu, B. Y. H.; Lee, K. W. An aerosol generator <strong>of</strong> high stability.<br />

Am. Ind. Hyg. J. 1975, 861-865.<br />

(3) Wang, S. C.; Flagan, R. C. Scanning electrical mobility analyzer.<br />

J. <strong>Aerosol</strong> Sci. 1989, 8, 1485-1488.<br />

(4) Collins, D. R.; Flagan, R. C.; Seinfeld, J. H. Improved inversion<br />

<strong>of</strong> scanning DMA data. <strong>Aerosol</strong> Sci. Technol. 2001, In press.<br />

(5) Rader, D. J.; McMurry, P. H. Application <strong>of</strong> <strong>the</strong> tandem<br />

differential mobility analyzer to studies <strong>of</strong> droplet growth or<br />

evaporation. J. <strong>Aerosol</strong> Sci. 1986, 17, 771-787.<br />

(6) Cocker, D. R.; Clegg, S. L.; Flagan, R. C.; Seinfeld, J. H. The effect<br />

<strong>of</strong> water on gas-particle partitioning <strong>of</strong> secondary organic<br />

aerosol: I. R-pinene ozone system. Atmos. Environ. 2001, In<br />

press.<br />

(7) Cruz, C. N.; Pandis, S. N. Deliquescence and hygroscopic growth<br />

<strong>of</strong> mixed inorganic-organic atmospheric aerosol. Environ. Sci.<br />

Technol. 2000, 34, 4313-4319.<br />

(8) Nenes, A.; Pandis, S. N.; Pilinis, C. ISORROPIA: A new <strong>the</strong>rmodynamic<br />

equilibrium model <strong>for</strong> multiphase multicomponent<br />

inorganic aerosols. Aquat. Geochem. 1998, 4, 123-152.<br />

(9) Bowman, F. M.; Odum, J. R.; Seinfeld, J. H.; Pandis, S. N.<br />

Ma<strong>the</strong>matical model <strong>for</strong> gas-particle partitioning <strong>of</strong> secondary<br />

organic aerosols. Atmos. Environ. 1997, 31, 3921-3931.<br />

Received <strong>for</strong> review November 29, 2000. Revised manuscript<br />

received April 3, 2001. Accepted April 5, 2001.<br />

ES0019169<br />

VOL. 35, NO. 12, 2001 / ENVIRONMENTAL SCIENCE & TECHNOLOGY 9 2601

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