3.101 A tank contains 0.5 m of nitrogen (N2) at -71°C and 1356 kPa. Determine the mass of nitrogen, in kg, using (a) the ideal gas model. (b) data from the compressibility chart. Comment on the applicability of the ideal gas model for nitrogen at this state.

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I need help for # 3.101. Thank you!
cially,
Working with the Ideal Gas Model
ment
3.100 For what
of
and temperature can air be
pressure
considered an ideal gas? Explain your reasoning. Repeat for
ranges
п an
onds.
H,O.
and
ided
3.101 A tank contains 0.5 m' of nitrogen (N2) at -71°C and
1356 kPa. Determine the mass of nitrogen, in kg, using
(a) the ideal gas model.
(b) data from the compressibility chart.
Comment on the applicability of the ideal gas model for
nitrogen at this state,
3.102 Determine the percent error in using the ideal gas model
to determine the specific volume of
(a) water vapor at 4000 Ibf/in.?, 1000°F.
(b) water vapor at 5 lbf/in.", 250°F.
(c) ammonia at 40 lbf/in., 60°F.
(d) air at 1 atm, 560°R.
(e) Refrigerant 134a at 300 lbf/in., 180°F.
3.103 Check the applicability of the ideal gas model for
(a) water at 600°F and pressures of 900 lbf/in. and 100
Ibf/in.2
(b) nitrogen at -20°C and pressures of 75 bar and 1 bar.
3.104 Determine the specific volume, in m/kg, of Refrigerant
134a at 16 bar, 100°C, using
H,0
(a) Table A-12.
Transcribed Image Text:cially, Working with the Ideal Gas Model ment 3.100 For what of and temperature can air be pressure considered an ideal gas? Explain your reasoning. Repeat for ranges п an onds. H,O. and ided 3.101 A tank contains 0.5 m' of nitrogen (N2) at -71°C and 1356 kPa. Determine the mass of nitrogen, in kg, using (a) the ideal gas model. (b) data from the compressibility chart. Comment on the applicability of the ideal gas model for nitrogen at this state, 3.102 Determine the percent error in using the ideal gas model to determine the specific volume of (a) water vapor at 4000 Ibf/in.?, 1000°F. (b) water vapor at 5 lbf/in.", 250°F. (c) ammonia at 40 lbf/in., 60°F. (d) air at 1 atm, 560°R. (e) Refrigerant 134a at 300 lbf/in., 180°F. 3.103 Check the applicability of the ideal gas model for (a) water at 600°F and pressures of 900 lbf/in. and 100 Ibf/in.2 (b) nitrogen at -20°C and pressures of 75 bar and 1 bar. 3.104 Determine the specific volume, in m/kg, of Refrigerant 134a at 16 bar, 100°C, using H,0 (a) Table A-12.
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