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Expert help when you need it- Q1: (Class Example) Consider a saturated liquid feed stream at 10 bar pressure, 10 kg/h. The stream consists of:Propane - 42 mol %, i-Butane - 10 mol%, n-butane - 45 mol %, n-pentane - 3 mol %. It is desired to flash this stream to a pressure of 5 bar and to separate 95% of the n-pentane via the product liquid stream. Determine the heat duty (MJ/h) in the flash unit needed to accomplish this operation.See Answer
- Q2: Consider a process with two sequential flash operations as shown below. The feed stream is at 100 °C, 3.8MPa. It consists of hydrogen-185 kmol/h, methane-45 kmol/h, benzene-45 kmol/h, toluene-5 kmol/h.The first flash column is operated at 100 °C with no pressure drop. The second flash column is operated adiabatically at 0.1 MPa pressure. Please select K and H value methods both as Peng-Robinson. a. What is the temperature of flash column 2? b. What are the molar fractions in the liquid product coming out of flash column 2? (Hint: you can set upstream molar fractions report) See Answer
- Q3: Consider a stream of the following chemical species: Hydrogen - 7 mol %, Methane - 85 mol %, Propane - 5mol%, i-Butane - 2.2 mol %, n-Hexane-0.8 mol %. K = SRK, H = SRK. a. What is the dew point temperature at 25 bar? b. What is the gas phase viscosity at saturation and 25 bar? What do you find when you try to determine the bubble point pressure at 40 °C? d. Can you explain why part (c) does not work by using the "Phase Envelope Plot" function in CHEMCAD? e. Can you determine the critical temperature and pressure using the plot in part (d)?See Answer
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