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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- For the following reaction set, define or propose two types of reactor systems to maximize product D selectivity, sketch the reactor system and describe clearly the input reactant concentrations and separation requirements if necessary. The unit of reaction rate is in units (mol/dm^3.sec) and concentration in units (mol/dm^3). (question on picture)arrow_forwardThe overall gas phase reaction 3A --> B + 2C occurs via the following sequence of elementary steps 2A <--> I1 + B k1,k-1 A + I1 --> 2I2 k2 I2 --> C k3 1. write an expression for the overall reaction rate, r, in terms of the rate step 3, r3 2. using the answer from 1, obtain an expression for the reaction rate, r, in terms of rate constants and concentrations of reactants and products, only use PSSH.arrow_forward1. Consider a gas-phase reaction, 2A - B +C + 3D with r = kC Initially 50% A and 50% inert are present. If the pressure and temperature remain constant, determine the final volume in terms of the initial and fractional conversion.arrow_forward
- Consider a gas-phase reaction, 2? → ? + ? + 3? with ?? = ??^2↓? Initially 50% A and 50% inert are present. If the pressure and temperature remain constant, determine the final volume in terms of the initial and fractional conversion.arrow_forwardGiven the following reactions, what is the enthalpy change for the reaction 3D -A+ 3B + 5C in kJ? (1) A- 3B + C, AH, = 100 kJ (2) A+C-D+B, AH, = -200 kJarrow_forwardConsider the reaction CaCO3(s)→CaO(s)+CO2(g).Estimate ΔG∘ and if they will be spontaneous for this reaction at 1475K, 1100K, & 295K. (Assume that ΔH∘ and ΔS∘ do not change too much within the given temperature range.)arrow_forward
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