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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- can you help with A and B My high school teacher said this is a good practice problemarrow_forward1,1,2 - trichloroethane - acetone solution containing 42% acetone by weight at a flow rate of 1200 kg/h will be extracted in a countercurrent multistage extraction system with water at a flow rate of 2100 kg/h at 25°C. The water is not pure and contains 2% by weight of 1.1.2-trichloroethane Since acetone in the raffinate phase is not to exceed 5% by weight; a. The amount and composition of the extract and raffinate phase, b. The percent recovery of acetone, c. Calculate the theoretical number of steps required. Extract Phase Refinate Phase 1,1,2- trichloroethane 1,1,2- acetone water acetone water trichloroethane 0.0596 0.0052 0.9352 0.0875 0.9093 0.0032 0.1704 0.0073 0.8223 0.2514 0.7376 0.0110 0.2692 0.0102 0.7206 0.3852 0.5921 0.0227 0.3088 0.0117 0.6795 0.4297 0.5392 0.0311 0.0426 0.0605 0.0890 0.3573 0.0160 0.6267 0.4821 0.4753 0.4090 0.0210 0.5700 0.5395 0.4000 0.4605 0.0375 0.5020 0.5740 0.3370 0.5178 0.0652 0.4170 0.6034 0.2626arrow_forward3. Determine the concentrations (in mole fraction) of all species in the exhaust from the complete combustion of propane (C3H8). Assume 50% excess air (79 mol% N2, 21 mol% O2) is the source for the охуgen.arrow_forward
- Calculate the formation volume factor for the gas given below for use at 5000 psig and 194 °F. Component Composition, mole percent Methane Ethane Propane i- Butane n-Butane - Pentane n-Pentane Нехапes Heptanes plus 97.12 2.42 0.31 0.05 0.02 trace trace 0.02 0.06 100.00 Properties of heptanes plus Soecific gravity Molecular weight 0.758 128 Iblb molearrow_forward4.1 If one mole of ethane, C2H6, is burned completely with 20 moles of air, what is the complete composition of the stack gas/flue gas?arrow_forwardChloroform (bp 61 °C) and methyl ethyl ketone (79 °C) form a maximum boiling azeotrope (bp 90 °C); the azeotropic mixture is 83% in methyl ethyl ketone (bp . SKETCH a distillation curve (volume on the x-axis and temperature on the y-axis) to show what you would expect to see should one distill 35 mL of a 50:50 mixture of these liquids. Be as quantitatively accurate as possible (using graph paper)arrow_forward
- Ethane reacts with pure oxygen to form water and carbon dioxide. If 3 moles of ethane and 12 mole of oxygen is mixed, and 80% of the ethane reacts, what is the percent excess of oxygen?A. 14.3%B. 20.5%C. 30.2%D. 50% Ans: A 14.3%arrow_forwardIf water contains about 42 mg of oxygen per liter at 20°C and 1.0 atm, what would be the value of Henry’s law constant for oxygen dissolving in water? The mole fraction of oxygen in the air is 0.21.arrow_forward5. Consider a mixture of 2 moles of 1-propanol and 8 moles of water at 1 atm (760 mmHg)(a) What would be the composition (mole fractions) of the liquid and gas phases if the system is maintained in equilibrium at 92.35 °C?(b) ) How many moles would be in each phase? Data on the system 1-propanol and water is presented in Figure 5 and Table VIII of: Murti, P., & Van Winkle, M. (1958). I have attached the table to this questionssarrow_forward
- Problem 1: The dimensionless Henry's law constant [air]/[water] for trichloroethylene (TCE) at 25°C is 0.4. A sealed glass vial is prepared that has an air volume of 4 mL overlying an aqueous volume of 36 mL. TCE is added to the aqueous phase so that initially it has an aqueous phase concentration of 100 ppb. After the system equilibrates, what will be the concentration (in units of ug/L) of TCE in the aqueous phase?arrow_forward1. Ethanol forms a nearly ideal solution with iso-butanol. The vapour-liquid equilibrium data is given below in terms of the more volatile component (ethanol).A heated feed containing 60mole % ethanol enters a flash drum at a rate of 50 kmol/h and equilibrium separation is achieved. What fraction of the feed to be vaporized to have a bottom product containing not more than 50% ethanol. 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 y* 0.196429 0.354839 0.485294 0.594595 0.6875 0.767442 0.836957 0.897959 0.951923 1arrow_forwardPlease use SI units and state which corellation is usedarrow_forward
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