Chapter 3: Problem 14
Determine the adiabatic, stoichiometric flame temperature at constant pressure for n-butanol, an alternative biofuel, give \((25 \mathrm{C}, 1 \mathrm{~atm})\) the enthalpy of combustion is \(-26\)
Chapter 3: Problem 14
Determine the adiabatic, stoichiometric flame temperature at constant pressure for n-butanol, an alternative biofuel, give \((25 \mathrm{C}, 1 \mathrm{~atm})\) the enthalpy of combustion is \(-26\)
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A steam boiler drum produces steam at a mass flow rate of \(64 \mathrm{~kg} \cdot \mathrm{s}^{-1}\) at 60 bar. This stream still contains \(2 \mathrm{wt} \%\) moisture. The feedwater from the economizer (a heat exchanger) is fed to the drum at a mass flow rate of \(62 \mathrm{~kg} \cdot \mathrm{s}^{-1}\). It contains \(3 \mathrm{ppm}_{\mathrm{w}}\) solids. Makeup water, containing \(50 \mathrm{ppm}_{\mathrm{w}}\) solids, is also fed into the drum at a mass flow rate of \(2 \mathrm{~kg} \cdot \mathrm{s}^{-1}\). Steam production is such that the solid content of the moisture leaving with the steam is \(5 \mathrm{ppm}_{\mathrm{w}}\). Blowdown, which is the release of hot liquid from the bottom of the drum, must keep the concentration of solids in the drum to \(1000 \mathrm{ppm}_{\mathrm{w}}\) - a. Calculate the blowdown requirement in \(\mathrm{kg} \cdot \mathrm{s}^{-1}\). b. Calculate the heat loss associated with blowdown in \(\mathrm{kW}\).
An anaerobic digester (see Chapter 14 for this technology) produces biogas at \(1.1\) bar (absolute) and \(25^{\circ} \mathrm{C}\). This gas, composed of 60 vol. \(\% \mathrm{CH}_{4}\) and 40 vol. \(\% \mathrm{CO}_{2}\), is to be compressed to 25 bar (absolute) before delivery to its end use; assume the compression to be isentropic and reversible. Calculate the temperature after compression.
Power company "E" in the Netherlands operates a fluidized bed combustion-based boiler with wood residues as fuel. The plant contains a simple steam turbine. The steam conditions at the inlet of the turbine are \(525^{\circ} \mathrm{C}\) and 100 bar. Assume that condensation of the steam takes place at a temperature of \(20^{\circ} \mathrm{C}\) and that isentropic expansion of steam occurs in the turbine. a. What is the specific power \(\left(\mathrm{kJ} \cdot \mathrm{kg}^{-1}\right)\) of the turbine expansion process? b. If the power plant generates \(25 \mathrm{MW}_{\mathrm{e}}\) and water pump work can be neglected, what is the mass flow rate of steam through the turbine? c. What assumptions have you made for these calculations?
What is the difference between an open system and a closed system?
Bio-oil flows through a duct with a radius of \(2.5 \mathrm{~cm}\) at ambient temperature with a velocity \(\left(\mathrm{v}_{1}\right)\) of \(10 \mathrm{~m} \cdot \mathrm{s}^{-1}\); the duct is followed by a permeable wall part with suction. At the end of this section (with the same radius), the velocity \(\left(\mathrm{v}_{2}\right)\) has dropped to \(8 \mathrm{~m} \cdot \mathrm{s}^{-1}\). If \(p_{1}=140 \mathrm{kPa}\), estimate \(p_{2}\) for the case that wall friction is negligible. What happens to \(p_{2}\) in the case of significant friction?
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