| 2D-3: | Volume Occupied by 10 kg of Water at Various Temperatures | 6 pts | |||||
| Determine the volume occupied by 10 kg of water at a pressure of 10 MPa and the following temperatures: | |||||||
| a.) | Ta | 5 | oC | ||||
| b.) | Tb | 200 | oC | ||||
| c.) | Tc | 400 | oC | ||||
| d.) | Td | 800 | oC | ||||
| e.) | Te | 1500 | oC | ||||
| f.) | Tf | -10 | oC | ||||
| Read : | This problem is an exercise in how to read and interpolate values from the Steam Tables. | ||||||
| It covers the use of the Subcooled Liquid Tables and the Superheated Vapor Tables, but does not involve double interpolation because the pressure value, 10 Mpa does appear explicitly in both the Subcooled Liquid and Superheated Vapor Tables. | |||||||
| Given : | m | 10 | kg | ||||
| P | 10 | MPa | |||||
| T | see the problem statement, above. | ||||||
| Find : | V | ??? | m3 | ||||
| Solution : | We need to determine the volume of the system and we are given the mass of water in the system. | ||||||
| We need to determine the specific volume of the system because : | |||||||
| Eqn 1 | |||||||
| So, for each part of this problem, we must evaluate the specific volume and plug this into Eqn 1 to determine the total volume of the system. | |||||||
| The first step in determining the specific volume is to determine the phase or phases present in the system. From the steam tables, we can obtain the saturation temperature associated with 10 Mpa. | |||||||
| Tsat | 311.1 | oC | |||||
| This makes it easy to determine the phase or phases in the system for each part of the problem. | |||||||
| If : | Tsys > Tsat | Then : | The system contains a superheated vapor. | ||||
| If : | Tsys < Tsat | Then : | The system contains a subcooled liquid. | ||||
| If : | Tsys = Tsat | Then : | The system could contain an equilibrium mixture of saturated liquid and saturated vapor. | ||||
| Part a.) | The system contains a subcooled liquid. Here are the key data values from the Subcooled Liquid Table of the Steam Tables : | ||||||
| T (oC) | V (m3/kg) | ||||||
| 0.01 | 0.0009952 | ||||||
| 20 | 0.0009973 | ||||||
| Eqn 2 | |||||||
| Eqn 3 | |||||||
| slope | 1.1E-07 | (m3/kg)/oC | |||||
| V | 0.0009957 | m3/kg | V | 0.009957 | m3 | ||
| Part b.) | The system contains a subcooled liquid. Here are the key data values from the Subcooled Liquid Table of the Steam Tables : | ||||||
| Tb | 200 | oC | V | 0.0011482 | m3/kg | ||
| No interpolation required ! | |||||||
| V | 0.011482 | m3 | |||||
| Part c.) | The system contains a superheated vapor. Here are the key data values from the Superheated vapor Table of the Steam Tables : | ||||||
| Tc | 400 | oC | V | 0.02644 | m3/kg | ||
| No interpolation required ! | |||||||
| V | 0.26436 | m3 | |||||
| Part d.) | The system contains a subcooled liquid. Here are the key data values from the Subcooled Liquid Table of the Steam Tables : | ||||||
| Td | 800 | oC | V | 0.04863 | m3/kg | ||
| No interpolation required ! | |||||||
| V | 0.48629 | m3 | |||||
| Part e.) | Te | 1500 | oC | ||||
| This temperature is too high for our steam tables ! | |||||||
| At very high temperatures, most gases behave as Ideal Gases. | |||||||
| The criterion by which we know it is reasonable to approximate real gases as ideal gases is : | |||||||
| Eqn 4 | |||||||
| The Ideal Gas EOS is : | Eqn 5 | ||||||
| or : | Eqn 6 | ||||||
| R | 8.314 | J/mole-K | V | 0.001474197 | m3/mole | ||
| V | 1.47 | L/mole | |||||
| The Ideal Gas EOS does NOT apply because V << 20 L/mole ! | |||||||
| Our only choice is to EXTRAPOLATE from the data in the steam tables. | |||||||
| That is not very safe and I do not want to encourage you to do this, so I will not do it here. | |||||||
| The best course of action is to find another data source. | |||||||
| Even the NIST Webbook only provides data up to 1001.9oC ! | |||||||
| This is not a good question ! | |||||||
| Part f.) | Tf | -10 | oC | ||||
| This value is too low for the Subcooled or Compressed Liquid Table ! | |||||||
| I do not recommend that you extrapolate. | |||||||
| This is not a good question ! | |||||||