Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN: 9781259696527
Author: J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher: McGraw-Hill Education
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- Please help me answer at least all of the given questions. Thank you.arrow_forward1) "Boiling Points" - Txy and xy diagrams. The vapor-pressure for the system n-octane & n-decane is available (spreadsheet): a) Using Raoult's Law and if needed Antoine's Equation calculate and plot the Txy diagram for a total pressure of 101.325kPa. b) Plot the xy data for this system at a total pressure of 101.325kPa.arrow_forward1) Ethanol-Water Separations. We wish to separate ethanol from water in a sieve-plate distillation column with a total condenser and a partial reboiler. There are two feed streams: Thermal State subcooled liquid* saturated vapor *Feed 2 condenses 0.25 moles of vapor for every mole of feed. The bottoms product should be 2% (mol) ethanol and the distillate should be 72% (mol) ethanol. Feed Flowrate (mol/hr) ZF 1 0.4 2 0.3 200 300 Notes: • The reflux ratio is equal to (1.0) and the feeds are to be input at their optimum location(s). • Both feeds are being input into the column, e.g. this is not intended to be solving for two unique columns but just one that has two input feed streams. • Equilibrium data for Ethanol-Water at 1 bar is shown in the table. You may also identify /use other experimental data (web sources, library) for this system. a) What are the flowrates of the distillate and bottoms products? b) What are the flowrates of liquid and vapor on stages between the two feeds…arrow_forward
- 1. Use the Chapman-Enskog theory and Fuller correlation to estimate the diffusion of hydrogen in nitrogen at 21°C and 2 atmospheres.arrow_forwardEthylene gas is converted ethanol compound by vapor phase hydration reaction. is being transformed. Maximum conversion amount at 523 K and 35 bar conditions, Calculate based on the amount of steam being 5 times the amount of ethylene. gas in equilibrium Assume that the mixture exhibits ideal solution behavior.arrow_forwardDraw a Pxy diagram for an aqueous solution of NH3. The temperature is such that the vapor pressure of the pure water is 5 kPa and the vapor pressure of pure NH3 is 600 Pa. You need to include the bubble line and the dew 7. line. (a) What is the vapor pressure of the solution when rNH, = 0.6? (b) In which phase the solution will be at P = 4.8 kPa? (c) In which phase the solution will be at P =0.2 kPa? (d) Draw the path for a process that takes a liquid with INH, = 0.6 %3D and P= 4.8 kPa to P= 0.2 kPa.arrow_forward
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