# Acharacteristic-Galerkin Aproximation to a system of Shallow by Dawson C.N., Martinez-Canales M.L.

By Dawson C.N., Martinez-Canales M.L.

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Additional info for Acharacteristic-Galerkin Aproximation to a system of Shallow Water Equations

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5 curve peaks at 410K. The lowering of the curve peaks partially offsets the additional energy necessary to warm the excess steam to operating temperatures. 5KJ to warm 1mole of water to 430K from room temperature. 5 moles of water to 410K from room temperature. ∆H = nC P ∆T (3. 1, and thus deep removal of CO to the parts per million (ppm) level is necessary [24] . The anode catalyst of the PEMFC is poisoned by only 10-40ppm CO [25,26] . 10 is a plot of CO in ppm. The CO curves were generated by multiplying by10,000 the CO mole fraction data.

The mole fraction has a dull apex around 400K that broadens with increasing steam in the feed gas. It is not difficult to ascertain the cause of the enhancement of H2 production with rising steam content. 4 confirms that all of the excess steam entering the reaction leaves the reaction. 5 moles of steam in the feed gas. 5 moles. 5 which is exactly the amount of the excess. Hence, for methanol, the stoichiometric excess steam acts so as to drive the reaction to completion to produce more H2 without participating in the reaction.

30 CO production from steam reforming of dimethyl ether at 1 bar varying steam to carbon ratio. More steam is needed to drive DME reforming to completion. 5 Conclusion A Comparison of the characteristics of each reforming fuel will determine how to best use the fuels to maximize H2 yield and minimize the CO content. 7%, with 13ppm of CO. 8ppm of CO. 7% yield, and 16ppm of CO. 1 Introduction Another effective means to generate hydrogen is from the pyrolysis of hydrocarbons. In the present chapter, the thermodynamic boundaries of the pyrolysis of methane and ethane are explored.