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Diffusion equations droplet phase reactions

The equations above have been the basis of most atmospheric aqueous-phase chemistry models that include mass transport limitations [e.g., Pandis and Seinfeld (1989)]. These equations simply state that the partial pressure of a species in the cloud interstitial air changes due to mass transport to and from the cloud droplets (incorporating both gas and interfacial mass transport limitations). The aqueous-phase concentrations are changing also due to aqueous-phase reactions that may be limited by aqueous-phase diffusion included in the factor Q. [Pg.574]

Vanag and Epstein have formulated a four-variable model to understand pattern formation in the BZ-AOT system [449,453]. Their model builds on the Oregonator, see Sect. 1.4.8. It assumes that the chemistry within the water core of the droplets is well described by the two-variable Oregonator rate equations (1.131). It further assumes that the species in the oil phase are inert, since they lack reaction partners, the key reactants all being confined to the aqueous core of the droplets. Consequently, only transfer reactions occur for the activator B1O2 and inhibitor Br2 in the oil phase. The rate terms for the two transfer reactions are added to the rate terms of the two-variable Oregonator model. The reaction-diffusion equations of the four-variable model of the BZ-AOT system are given in nondimensionalized form by... [Pg.357]


See other pages where Diffusion equations droplet phase reactions is mentioned: [Pg.78]    [Pg.76]    [Pg.233]    [Pg.755]    [Pg.55]    [Pg.601]    [Pg.615]    [Pg.153]    [Pg.306]    [Pg.616]    [Pg.627]    [Pg.632]    [Pg.473]    [Pg.584]    [Pg.483]    [Pg.4674]   
See also in sourсe #XX -- [ Pg.139 , Pg.140 ]




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