Lithium-Sulfur Battery: Design, Characterization, and Physically-based Modeling

PDF Publication Title:

Lithium-Sulfur Battery: Design, Characterization, and Physically-based Modeling ( lithium-sulfur-battery-design-characterization-and-physicall )

Previous Page View | Next Page View | Return to Search List

Text from PDF Page: 075

mass-action kinetics. For each reaction q, the term s ̇n,q is defined as 􏰜􏰝 s ̇ =ν k an′ −kq,rev ∏an′′ , (4.6) n,q n,q q,fwd ∏ νn′,q νn′′,q n′ ∈q, fwd n′′ ∈q, rev where kfwd and krev are the forward and backward rate constants, νn the stoichiometric coefficients of species n in the corresponding reaction q, and an the activities. The products run over all reactants n′ or n′′ participating in the forward or reverse reaction, respectively. The total production rate of species n at interface m is simply the sum of the contributions of all reactions q at that interface: s ̇n,m = ∑ s ̇n,q . (4.7) q∈m The equation for bulk reactions has exactly the same form, except that the units of activities and rate constants differ, so that s ̇n is a volume-specific production/ consumption rate instead of an area-specific one. The forward rate constant is given by a general modified Arrhenius expression (index q omitted in the following equations): ̃ 􏰘 Eact􏰙 􏰘 (1−α)zF 􏰙 kfwd = k0,fwdTβ exp − RT exp − RT ∆φ . (4.8) Since there is no reason to assume otherwise, the symmetry factor α is chosen to be 1/2 for all reactions. Also, because the model is assumed strictly isothermal, both the temperature factor Tβ and the activation energy Eact may be eliminated so that Eq. (4.8) is reduced to 􏰘 zF 􏰙 kfwd = k0,fwd exp −2RT∆φ , (4.9) with z being the number of electrons transferred, F Faraday’s constant, R the uni- versal gas constant, T the (now fixed) temperature, and ∆φ the potential step at the corresponding interface: ∆φ = φelde − φelyte. The pre-exponential factor k0, fwd now incorporates the contributions of the two temperature-dependent terms in Eq. (4.8), which are reduced to a fixed factor in the case of constant temperature. For mere chemical reactions (i.e. z = 0), kfwd is equal to k0, fwd. While reverse reactions rates may be specified analogously, i.e. in the form 􏰘zF 􏰙 krev = k0, rev exp 2RT ∆φ , (4.10) this is not the case for most reactions in this model. Instead, reverse rates are calculated 75

PDF Image | Lithium-Sulfur Battery: Design, Characterization, and Physically-based Modeling

PDF Search Title:

Lithium-Sulfur Battery: Design, Characterization, and Physically-based Modeling

Original File Name Searched:

Dissertation_David_N._Fronczek_The_Lithium_Sulfur_Battery.pdf

DIY PDF Search: Google It | Yahoo | Bing

Sulfur Deposition on Carbon Nanofibers using Supercritical CO2 Sulfur Deposition on Carbon Nanofibers using Supercritical CO2. Gamma sulfur also known as mother of pearl sulfur and nacreous sulfur... More Info

CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info

CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com (Standard Web Page)