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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- To make an 18.76% (w/w) solution, what volume (mL) of solvent would be needed for a solution that contains 12.58 grams of solute? The density of solvent is 1.246 g/mL and the molecular weight of the solute is 54.12 g/mol. 38.2 mL 54.5 mL 43.7 mL O 21.8 mL Next by ProProfs Create a Quiz rch 24% 27°C Sunny O D E 4)) G ENarrow_forward03: A sample of natural gas from the Texas field has the specific gravity 0.712(air-1), this gas contains nonhydrocarbon compounds (carbon dioxide, nitrogen and hydrogen sulfide) around (1.9,2.45,11.13) mole % respectively. By using appropriate equations find the gas deviation factor at reservoir temperature 215 °F and pressure 2395.30 psig. Component CH4 C₂H6 C3H8 i-C4H10 N₂ CO₂ H₂S 16.043 30.070 44.097 58.124 28.01 44.01 34.08 493 1071 227 574 Mole Weight Pri psia Tai R 668 343 708 550 616 666 529 735 1306 624arrow_forward4. [Scrubber]. A coal-fired combustion system produces flue gas that contains particulate matter. To reduce the amount of particles, the flue gas is treated in a scrubber. The measurement of the mass and size of the particles at the inlet and outlet of the scrubber yielded the size distribution data given in the following table: Particle diameter [um] (size interval: dlower → dupper) 0.10.25 0.25 → 0.5 0.5 → 1.0 1.0→2.0 2.05.0 Formulas for question 4: . Particle mass at scrubber inlet [mg] 623 55.4 12.6 8.9 7.1 5.0 10 7.7 10 →30 6.6 30→ 50 4.3 The mass of particles in each size interval was measured on a basis of 1 m²³. 31.4 33.2 123 a) What is the overall efficiency of the scrubber? [Ans: noverall 96.7 %] b) Calculate the collection efficiency (na,i) of the scrubber and the particle geometric average diameter (dpi) for each size interval. Create a graph showing the variation of na,i with dp,i. (PTO) efficiency: nd,i (%) = - 394 775 1055 c) Calculate the mass-average diameter of the…arrow_forward
- Titanium dioxide (TIO:) is used extensively as a white pigment. It is produced from an ore that con- tains ilmenite (FETIO,) and ferric oxide (Fe,0,). The ore is digested with an aqueous suifuric acid solution to produce an aqueous solution of titanyl sulfate [(TiO)SO.] and ferrous sulfate (FeSO,). Water is added to hydrolyze the titanyl sulfate to H;TIO3, which precipitates, and H2SO.. The pre- cipitate is then roasted, driving off water and leaving a residue of pure titanium dioxide. (Several steps to remove iron from the intermediate solutions as iron sulfate have been omitted from this description.) Suppose an ore containing 24.3% Ti by mass is digested with an 80% H;SO, solution, supplied 50% excess of the amount needed to convert all the ilmenite to titanyl sulfate and all the ferric oxide to ferric sulfate [Fe;(SO,)). Further suppose that 89% of the ilmenite actually decomposes. Calculate the masses (kg) of ore and 80% sulfuric acid solution that must be fed to produce 1000 kg…arrow_forward29.2 Hydrogen sulfide (H₂S) is a common contaminant in natural gas. The dissolution of H₂S gas in water is a linear function of partial pressure, as is described by Henry's law of the form PA = H x. Values of H vs. temperature are provided below: T (°C) H (atm) mole H₂S/ mole MEA 20 483 PA (mm Hg) 30 449 Given the relatively low solubility of H₂S in water, an amine- based chelating agent is added to the water to improve the solubility of H₂S. Equilibrium distribution data for H₂S in a 15.9 wt% solution of monoethanolamine (MEA) in water at 40°C is provided below: 40 520 50 577 0.000 0.125 0.208 0.362 0.643 0.729 0.814 0.00 0.96 3.00 9.10 43.1 59.7 106 Describe the effect of temperature on the solubility of H₂S gas in water. b. Prepare equilibrium distribution plots, in mole-fraction coordinates (y₁ -— XÃ), for the solubility of H₂S in water vs. H₂S in 15.9 wt% MEA solution at 40°C and 1.0 atm total system pressure. Comment on the relative solubility of H₂S in water vs. MEA solution.arrow_forwardA continuous fractionating column is required to separate a binary mixture containing 0.20 mole fraction of A into a top product of 0.95 mole fraction A, and a bottom product containing 0.02 mole fraction A. The feed is liquid at its boiling point. The vapour leaving the column is condensed but not cooled, and the reflux ratio is 9:1. The relative volatility (a) remains constant at 1.85 and the vapour and liquid equilibrium data are in the form: α = y(1-x) x(1-y) Calculate: (a) the number of theoretical plates required; (b) the position of the feed plate;arrow_forward
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