Chapter 8: Problem 13
Miao et al. (2011) show a correlation between the bulk density of biomass and the screen size as a power law expression. Why is the correlation characterized by a negative sign in the power of the characteristic size?
Chapter 8: Problem 13
Miao et al. (2011) show a correlation between the bulk density of biomass and the screen size as a power law expression. Why is the correlation characterized by a negative sign in the power of the characteristic size?
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A certain type of straw (with 15 wt\% moisture content) is submerged in water at a mass ratio of water to straw of 4 . The straw initially contains \(0.8 \mathrm{wt} \% \mathrm{Cl}\) (ar basis). When taken out of the water, the straw is very wet with a moisture content of \(80 \mathrm{wt} \%\) but a \(\mathrm{Cl}\) content of only \(0.03 \mathrm{wt} \%\). What is the partitioning coefficient of \(\mathrm{Cl}\) when this is defined as the mass fraction of \(\mathrm{Cl}\) in the water phase divided by the \(\mathrm{Cl}\) mass fraction in the wet biomass before submerging? What do you assume?
Which factors cause emissions of VOCs to increase when using direct drying techniques?
In practice, is screening always needed for biomass processing?
A wood drying system consists of boiler in which dried wood (with 25 wt\% moisture content) is burned with ambient air \(\left(25^{\circ} \mathrm{C}\right)\) and hot water is generated. The flue gas available at \(130^{\circ} \mathrm{C}\) (immediately after the boiler) is used to dry the wood from \(55 \mathrm{wt} \%\) moisture content in an integrated manner. The wood enters the dryer at \(25^{\circ} \mathrm{C}\). The initial LHV of the wood is \(9.5 \mathrm{MJ} \cdot \mathrm{kg}^{-1}\) (ar) and the wet wood feed rate is \(250 \mathrm{~kg} \cdot \mathrm{h}^{-1}\). Consider a combustion system in which combustion with \(25 \%\) excess air is applied. Use the wood composition for pellets (daf basis) presented in Table \(2.3\). The boiler and dryer may be assumed to have no heat losses. The \(\mathrm{c}_{\mathrm{p}}\) value of wood can be assumed to be constant at \(1200 \mathrm{~kJ} \cdot \mathrm{kg}^{-1} \cdot \mathrm{K}^{-1}\). a. Which type of dryer do you prefer for this system and why? b. What must be the capacity of the air fan (in \(\mathrm{kg} \cdot \mathrm{h}^{-1}\) )? c. What is the amount of heat transferred per unit of time to the water system in the boiler? d. What is the end temperature of the flue gas after the dryer? e. Is the temperature at the dryer exit above the dew point of the water?
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