Chapter 11: Problem 3
The concentration of acetic acid in pyrolysis oil varies between 1 and the \(8 \mathrm{wt} \%\). HAc is the most abundant acid in the oil. Can you explain the low (2-3) but hardly varying \(\mathrm{pH}\) of the oil?
Chapter 11: Problem 3
The concentration of acetic acid in pyrolysis oil varies between 1 and the \(8 \mathrm{wt} \%\). HAc is the most abundant acid in the oil. Can you explain the low (2-3) but hardly varying \(\mathrm{pH}\) of the oil?
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Get started for freeFor the case where sand is circulated between a hot utility and the pyrolysis reactor, derive an equation that gives the required sand flow (in \(\mathrm{kg}\) ) per \(\mathrm{kg}\) biomass fed as a function of the temperature differences between the pyrolysis reactor and the hot utility and the energy requirement of the reactor.
Calculate the amount \((\mathrm{kg})\) of \(\mathrm{H}_{2}\) needed per \(\mathrm{kg}\) product for complete deoxygenation of pyrolysis oil and discuss the economics of the process based on this number.
a. Explain why the observation of larger oligomers during the pyrolysis of a cellulose particle contradicts an unzipping mechanism. b. Argue how these large oligomer anhydrosugars \((D P=9)\) leave the particle.
a. Derive an expression that relates the loss of vapors due the homogeneous vapor cracking reaction in the hot zone above a fluidized bed as a function of temperature and vapor residence time. b. Consider a fluidized bed pyrolysis reactor that contains ideally mixed biomass particles that are producing vapors. In the fluidized bed reactor, also, vapor cracking proceeds, which can be described by a first-order reaction in vapors. Derive an expression to calculate the fraction of the vapors that is cracked relative to the amount produced in the pyrolysis reactions as a function of temperature and residence time. You may assume that the gas/vapors show plug flow behavior.
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