Chapter 8: Problem 8
Which particle properties change when size reduction is applied?
Chapter 8: Problem 8
Which particle properties change when size reduction is applied?
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Get started for freeIn practice, is screening always needed for biomass processing?
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?
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?
List advantages and disadvantages of direct comilling of biomass with coal. Is this always possible?
Describe the pros and cons of direct drying using flue gas and steam.
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