| 2F-2 : | An Application of Equations of State | 6 pts | |||||||
| Ten kilograms of 600oC steam is contained in a 182 L tank. Find the pressure using: | |||||||||
| a.) | The Ideal Gas EOS | ||||||||
| b.) | The van der Waal EOS | ||||||||
| c.) | The Soave-Redlich-Kwong EOS | ||||||||
| d.) | The Compressibility Factor EOS | ||||||||
| e.) | The Steam Tables | ||||||||
| Read : | Not much to say here. | ||||||||
| Given : | m | 10 |
kg | V | 182 |
L | |||
| T | 600 |
oC | 0.182 |
m3 | |||||
| Part a.) | Ideal Gas EOS : | Eqn 1 | Solve for pressure : | Eqn 2 | |||||
| We must determine the molar volume before we can use Eqn 2 to answer the question. | |||||||||
| Use the definition of molar volume: | Eqn 3 | ||||||||
| Where : | Eqn 4 | ||||||||
| MW | 18.016 |
g H2O / mol H2O | n | 555.06 |
mol H2O | ||||
| V | 3.28E-04 |
m3/mol | |||||||
| Now, plug values back into Eqn 2. | R | 8.314 |
J/mol-K | ||||||
| Be careful with the units. | T | 873.15 |
K | ||||||
| P | 2.21E+07 |
Pa | |||||||
| Answer : | P | 22.1 |
MPa | ||||||
| Part b.) | van der Waal EOS : | Eqn 5 | |||||||
| We can determine the values of a and b, which are constants that depend only on the chemical species in the system, from the following equations. | |||||||||
![]() |
Eqn 6 | Tc | 647.4 |
K | |||||
| Pc | 2.21E+07 |
Pa | |||||||
| a | 0.5530 |
Pa-mol2/m6 | |||||||
| Eqn 7 | b | 3.04E-05 |
m3/mol | ||||||
| Now, we can plug the constants a and b into Eqn 5 to determine the pressure. | |||||||||
| Answer : | P | 19.3 |
MPa | ||||||
| Part c.) | Redlich-Kwong EOS : | ![]() |
Eqn 8 | ||||||
| We can determine the values of a, b and α, which are constants that depend only on the chemical species in the system, from the following equations. | |||||||||
![]() |
Eqn 9 | Eqn 10 | |||||||
| Now, plug values into Eqns 8 -10 : | |||||||||
| a | 14.25855 |
Pa-m6-K1/2/mol2 | b | 2.110E-05 | m3/mol | ||||
| Answer : | P | 19.4 |
MPa | ||||||
| Part d.) | Compressibility EOS : | Given TR and the ideal reduced molar volume, use the compressibility charts to evaluate either PR or the compressibility, Z | |||||||
![]() |
Eqn 11 | Eqn 12 | |||||||
| TR | 1.3487 | ||||||||
| Defiition of the ideal reduced molar volume : | ![]() |
Eqn 13 | |||||||
| VRideal | 1.3463 | ||||||||
| Read the Generalized Compressibility Chart for PR = 0 to 1 : | PR | 0.88 | |||||||
| Z | 0.885 | ||||||||
| We can use the definition of PR to calculate P : | Eqn 14 | ||||||||
| Eqn 15 | |||||||||
| Answer : | P | 19.4 |
MPa | ||||||
| Or, we can use Z and its definition to determine P : | ![]() |
Eqn 16 | |||||||
| Answer : | P | 19.6 |
MPa | ||||||
| Part e.) | The Steam Tables provide the best available estimate of the pressure in the tank. | ||||||||
| Because T > Tc, the properties of the water in the tank must be obtained from the superheated vapor table, even though the water is actually a supercritical fluid in this system. | |||||||||
| At this point we can make use of the fact that we have a pretty good idea of what the actual pressure is in the tank (from parts a-d) or we can scan the spuerheated vapor tables to determine which two pressures bracket our known value of the specific volume. | |||||||||
| In either case, we begin by converting the molar volume into a specific volume : | |||||||||
| Eqn 17 | |||||||||
| Using the MW of water from part a yields : | v | 1.820E-05 |
m3/g | ||||||
| v | 1.820E-02 |
m3/kg | |||||||
| The Superheated Steam Table gives us : | |||||||||
| At P = | 15 |
MPa | and | At P = | 20 | MPa | |||
| v = | 0.02491 |
m3/kg | v = | 0.01818 | m3/kg | ||||
| Answer : | We can determine the pressure in our tank by interpolation : | P | 19.99 | MPa | |||||
| P | 20.0 |
MPa | |||||||





