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Open AccessJournal Article

Nitric oxide (NO) reduction by retorted oil shale

R.W. Taylor, +1 more
- 01 Jan 1984 - 
- Vol. 29, Iss: 1, pp 277-283
TLDR
In this article, it was shown that the reduction rate of NO appears to be proportional to the partial pressure of NO, and the results can be expressed in terms of a rate constant (k) which is a function of temperature (T, Kelvin).
Abstract
Nitric oxide gas (NO) is effectively reduced by retorted oil shale. At 300/sup 0/C half of the NO in a gas stream is removed when the gas stream contacts a bed of crushed retorted oil shale for 0.4 s. The fraction removed in 0.4 s reaches 90% at a temperature of 375/sup 0/C. As long as the reducing agent, presumed to be char in the retorted shale, is not depleted, the rate of reduction of NO appears to be proportional to the partial pressure of NO, and our results can be expressed in terms of a rate constant (k) which is a function of temperature (T, Kelvin) as follows: k = Ae/sup -//sup E/RT/ (s/sup -1/), where A = 4.0 x 10/sup 5/ (s/sup -1/) and E = 59.7 kJ/mole. This rate is many times faster than the rate of reduction of NO by coal char as measured by Furusawa et al. (1983). The principal reduction reaction is unknown; it does not release CO/sub 2/.

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References
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Journal ArticleDOI

Kinetics of the NOcarbon reaction at fluidized bed combustor conditions

TL;DR: In this article, the reduction of NO by carbonaceous solid has been studied in a packed bed reactor, and the reaction rate per unit total surface area is found to be first order in NO, to have an apparent activation energy of 44 kcal/mole for temperatures higher than 873K, enhanced by the presence of CO, and to vary by approximately an order of magnitude between graphite and coal chars.
Journal ArticleDOI

22 Nox emission control from a fluidized bed combustor of coal: Effects of in situ form char on “NO” reduction

TL;DR: In this paper, the kinetic behavior of the reaction in the presence of oxygen was investigated by means of a fixed bed reactor at a temperature of 500-680°C as well as a fluidized bed at a level of 600-800°C.