Chapter 10: Problem 13
Recap the pros and cons of the use of circulating fluidized bed gasifiers versus entrained flow gasifiers.
Chapter 10: Problem 13
Recap the pros and cons of the use of circulating fluidized bed gasifiers versus entrained flow gasifiers.
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For Example \(10.2\), check whether the criterion for negligible intraparticle heat transfer limitation is fulfilled. Take \(\Delta_{\mathrm{r}} \mathrm{H}=227.5 \mathrm{~kJ} \cdot \mathrm{mol}^{-1}\) and \(\mathrm{E}_{\mathrm{a}}=\) \(220 \mathrm{~kJ} \cdot \mathrm{mol}^{-1}\). Assume the gas properties are those of pure nitrogen at \(900^{\circ} \mathrm{C}\). These are \(\lambda=0.074 \mathrm{~W} \cdot \mathrm{m}^{-1} \cdot \mathrm{K}^{-1}, \rho=0.2875 \mathrm{~kg} \cdot \mathrm{m}^{-3}\), and \(\mathrm{c}_{\mathrm{p}}=1.199 \mathrm{~kJ} \cdot \mathrm{kg} \cdot \mathrm{K}^{-1}\).
In a BFB gasifier, biomass fuel can be fed from the top or from the bottom part (in-bed feeding); what are the implications of these different ways of feeding for the gas composition?
Which problems do you foresee when applying SCW gasification with seaweed (macroalgae) as feedstock?
Why does a model based on chemical equilibrium calculations predict higher \(\mathrm{CH}_{4}\) formation at higher pressure and typical fluidized bed gasifier temperatures of about \(850^{\circ} \mathrm{C}\) ?
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