Chapter 8: Problem 11
How can particle size distributions be determined? Which average particle sizes can you name? Why are they needed?
Chapter 8: Problem 11
How can particle size distributions be determined? Which average particle sizes can you name? Why are they needed?
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Get started for freeA 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?
What are advantages and disadvantages of compacting biomass?
Which particle properties change when size reduction is applied?
What are limits in the application of mechanical dewatering of biomass?
A community intends to use their sewage waste (using urine separation) to derive energy from it. The material is very wet, however, and even with urine separation, only about \(29 \mathrm{wt} \%\) dry matter can be obtained. About 700 households produce \(125 \mathrm{~kg}\). day \({ }^{-1}\) of feces matter, and the combustion process that is to be applied requires 80 wt \(\%\) dry matter material. a. How much water must be removed per second in a continuous process? b. In case no heat losses occur, what would be the energy needed for this drying process? Neglect the heating up of the feces, but only consider the water heat up and evaporation at atmospheric conditions. c. Would the assumption in (b) lead to a large difference in the calculated heat supply?
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