17.10 - Solving Equilibria for Multiple Reactions
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- Chapter 1 - Basic concepts
- Chapter 2 - The energy balance
- Chapter 3 - Energy balances for composite systems.
- Chapter 4 - Entropy
- Chapter 5 - Thermodynamics of Processes
- Chapter 6 - Classical Thermodynamics - Generalization to any Fluid
- Chapter 7 - Engineering Equations of State for PVT Properties
- Chapter 8 - Departure functions
- Chapter 9 - Phase Equlibrium in a Pure Fluid
- Chapter 10 - Introduction to Multicomponent Systems
- Chapter 11 - An Introduction to Activity Models
- Chapter 12 - Van der Waals Activity Models
- Chapter 13 - Local Composition Activity Models
- Chapter 14 - Liquid-liquid and solid-liquid equilibria
- Chapter 16 - Advanced Phase Diagrams
- Chapter 15 - Phase Equilibria in Mixtures by an Equation of State
- Chapter 17 - Reaction Equilibria
- Chapter 18 - Electrolyte Solutions
Multiple Reaction Equilibria using Excel (8:48)
Multiple Reaction Equilibria using Excel (8:48) (msu.edu)
Example 17.6 (Section 17.10) solves two reactions for equilibrium simultaneously with Excel. To skip the problem set up and see how to use Excel variables jump to 5:15. To jump to the use of solver for two equations, jump to 7:15.
Comprehension Questions:
1. CH3OH is fed to a reactor at 200ΒΊC and 3 bar with a catalyst that produces CO, H2, dimethyl ether, and H2O. Calculate the equilibrium extents of reaction and compositions of all species.
2. Diisopropylbenzene (DIPB) is a possible byproduct of the reaction of benzene with propylene to make cumene. If the reaction is conducted at 300C and 11 bars with a stoichiometric feed relative to the cumene reaction, calculate the equilibrium extents of reaction and compositions of all species.