Chapter 11: Problem 6
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.
Chapter 11: Problem 6
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.
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Get started for freeThe 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?
For 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.
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.
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.
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