Sustainable Energy
2nd Edition
ISBN: 9781337551663
Author: DUNLAP, Richard A.
Publisher: Cengage,
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Chapter 4, Problem 12P
(a)
To determine
Find the mass of
(b)
To determine
Determine the density of
Determine the size of the cubic container.
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A gas undergoes a cycle in a piston-cylinder assembly consisting of the following three processes:
Process 1-2: Constant pressure, p = 1.4 bar, V₁ = 0.028 m³, W12 = 10 kJ
Process 2-3: Compression with pV = constant, U3 = U₂
Process 3-1: Constant volume, U₁ - U3 = -25 kJ
There are no significant changes in kinetic or potential energy.
(a) Calculate the net work for the cycle, in kJ.
(b) Calculate the heat transfer for process 1-2, in kJ.
Part A
Your answer is correct.
Calculate the net work for the cycle, in kJ.
Wcycle = -7.63
kJ
The Bunsen burner in your labs are fueled by natural gas, which is mostly methane, CH4. The
thermochemical equations for the combustion of methane (burning in oxygen) is:
CH4(g) + 2 O2(g) ➔ CO2(g) + 2 H2O (g) ΔH = – 890.3 kJ/mole
Calculate ΔH in kJ when 5.00 g CH4 react with an excess oxygen.
Cellulose is to be burned in a waste to energy facility. The chemical equation for cellulose is C6H10O5. The atomic weights of C, H, and O are 12, 1, and 16, respectively. The ideal equation for the combustion of cellulose is C6H10O5 +6O2à6CO2 + 5H2O.
Calculate the stoichiometric oxygen necessary for the combustion of cellulose.
Calculate the stoichiometric air supply. The air is 23.15% oxygen by weight.
If the facility operates at 1.5 tons/hour at 100% excess air. How much air is required?
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