By Peter Auer and David Douglas (Eds.)

ISBN-10: 0120149044

ISBN-13: 9780120149049

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**Sample text**

Rotty Rotty, R. M. (1973). Commentary on and extension of calculative pro cedure for C0 2 production. Tellus 25(5), 508-517. Rotty, R. M. (1979). Present and future production of C0 2 from fossil fuels—A global appraisal. In Elliot and Machta, op. , pp. 36-43. Rotty, R. M. (1983). Distribution of and changes in industrial carbon dioxide production. / . Geophys. Res. 88(C2), 1301-1308. Rust, B. , Rotty, R. , and Marland, G. (1979). Inferences drawn from atmospheric C0 2 data. / . Geophys. Res. 84(C6), 31153122.

Between the species can be characterized many different ways. The associated equilibrium constants determine the proper coefficients in the above chemical equation. The answers one finally obtains are unique and independent of the choice of combination of equilibrium constants (they are all related to one another). We choose the following reactions and associated equilibrium constants. C0 2 ±5 CO + έ0 2 Κχ = PcoPo22'Pco2 (14) H 2 0 ±5 H2 + K)2 K2 = pH2p^/pH20 (15) CO + NO ±* C0 2 + έΝ2 Κ3 = PCO2PN22/(PCOP^O) (16) CO + OH ±5 C0 2 + iH2 K4 = PCO2PH2/(PCOPOH) (17) These equilibrium constants, mass conservation and the choice of the final temperature, pressure, and the initial air-fuel ratio determine the final composition of the combustion products.

375(1 - φ)1/2 exp(-10,750/J) (29) In Eq. (29) T depends on φ and is a maximum at φ = 1. Note that the general features of the equilibrium [NO] concentration are such that [NO] is not large at small φ because the T in the exponential is small if one burns a very lean mixture. As φ increases, T increases so the exponential term gets larger, but the available oxygen [02] is becoming less. Thus the [NO] will peak at some φ < 1. This approximation puts [NO] = 0 at φ = 1, which is not true, but is due to our simplified manipulations for lean mixtures.

### Advances in Energy Systems and Technology. Volume 4 by Peter Auer and David Douglas (Eds.)

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