ENGR266 Summer 2021 Q1[PARTIAL] Left out: Parts (b)-(c) need the Pitzer second-virial correlation and the generalised compressibility chart, which are not in the current slides or formula sheets (only Z, van der Waals and Redlich-Kwong are taught).
Answer ALL parts (a) - (c).
Formulas you may need
- SFEE: (on the formula sheet)
- Liquid enthalpy change: (from , ) (on the formula sheet)
- Compressibility factor: , reduced properties , (learn this)
- [EXTERNAL] Pitzer second-virial correlation: , , , (learn this; not in the current materials)
- [EXTERNAL] Lee-Kessler corresponding states: with read from the Lee-Kessler tables (learn this; not in the current materials)
- (a)[7]2:2Water in a tank at is pumped into a second tank that is located 20 m above the initial tank at a rate of . The pump does of work and the water loses of heat during the transfer. Assuming that the specific heat of water is , calculate the temperature of the water in the second tank, stating any assumptions made.
- (b(i))[6]2:2Calculate the compressibility factor for methanol at a temperature of and a pressure of 404.85 bar using the Pitzer Correlation for the Second Virial Coefficient. For methanol the critical temperature and pressure are and 80.97 bar respectively and the acentric factor is 0.354.
- (b(ii))[2]2:2Calculate the same compressibility factor using the theorem of corresponding states.
- (c)[4]Comment on differences between the two numbers and discuss their reliability.