Partially Miscible & Immiscible Solutions Contributions by: John L. Falconer & Will Medlin Department of Chemical and Biological Engineering University.

Slides:



Advertisements
Similar presentations
Properties of a Pure Substance
Advertisements

Use of Steam Tables Saturated Vapor or Liquid
Gas Solubilities Henry’s Law: [A]equilibrium = SA · pA
Reversible & Irreversible Processes
APPLICATIONS Applications of Raoult’s law
First Law of Thermodynamics
Solutions Contributions by:
Entropy Contributions by:
Goal 1: Design a flash drum
First Law of Thermodynamics Part 2
Chemical Equilibrium Chapter 6 pages Reversible Reactions- most chemical reactions are reversible under the correct conditions.
H+H+ H+H+ H+H+ OH - New Way Chemistry for Hong Kong A-Level Book 2 1 Chapter 21 Phase Equilibrium I: One-Component Systems 21.1Definition of a Phase 21.2Phase.
PETE 310 Lectures # 6 & # 7 Phase Behavior – Pure Substances (Lecture # 5) Two Component Mixtures Three & Multicomponent Mixtures.
Fugacity Contributions by:
Chapter 12 Gas-Liquid Equilibrium
Equilibrium: The Story So Far… Condensed Phase Dispersed Phase Pure liquid or solid (l), (s) The rate of particles leaving the system does not depend.
PETE 310 Lectures # 32 to 34 Cubic Equations of State …Last Lectures.
Solutions – homogeneous mixtures that can be solids, liquids, or gases
Solid-vapor equilibrium (SVE) and Solid-liquid equilibrium (SLE)
Chapter 14-Part VII Applications of VLLE.
Chapter 14: Phase Equilibria Applications
1 Boyle’s Law (T and n constant) Charles’ Law (p and n constant) Combined Gas Law (n constant) Summary of Gas Laws p 1 ×V 1 = p 2 ×V 2.
Section 4 -Phase Equilibrium Two-Phase Systems A system is a set of components that are being studied. Within a system, a phase is a region that has the.
Solution Thermodynamic:
First Law of Thermodynamics
Properties of Pure Substances
THERMODYNAMICS LAB Properties of Pure Substances
FLASH CALCULATION A flash is a single-equilibrium stage distillation in witch a feed is partially vaporized to give a vapor richer in the most volatile.
Liquid - Liquid Phase Diagrams
Physical Chemistry I (TKK-2246)
Vapor pressure and liquids Vapor : A gas that exists below its critical point Gas : gas that exists above its critical point ِNote : A gas can not condense.
Scheme of the equilibrium Environmental Compartments Model.
Chemical Equilibrium Contributions by: John L. Falconer & Will Medlin Department of Chemical and Biological Engineering University of Colorado Boulder,
Phase Equilibrium: Two Components
Phase Equilibrium: Two Components in Piston-Cylinders
Phase Equilibrium: Two Components in Piston-Cylinders Contributions by: John L. Falconer & Will Medlin Department of Chemical and Biological Engineering.
Chemical Equilibrium Contributions by: John L. Falconer & Will Medlin Department of Chemical and Biological Engineering University of Colorado Boulder,
Cycles Contributions by:
OTHER CONCENTRATION UNITS Yves Alarie, Ph.D Professor Emeritus U niversity of Pittsburgh,USA.
Solutions Homogeneous mixtures that may be solid, liquid or gaseous Solute: The part of the solution that is dissolved Solvent: The part of the solution.
VAPOR/LIQUID EQUILIBRIUM- Introduction
Ideal Gases Contributions by:
Miscellaneous Contributions by:
Phase Changes Contributions by:
Solution thermodynamics theory—Part I
Phase Equilibrium: Single Condensable Component Part 2
Phase Equilibrium: Two Components
Dalton’s law of partial pressure At constant volume and temperature, the total pressure of a mixture of gases is the sum of the partial pressures of all.
Two-Phase Gas-Liquid Systems (Saturation, Condensation, Vaporization) Saturation  When any noncondensable gas (or a gaseous mixture) comes in contact.
Phase Equilibrium: Single Condensable Component Part 1
Fugacity Contributions by: John L. Falconer & Will Medlin Department of Chemical and Biological Engineering University of Colorado Boulder, CO
APPLICATIONS Applications of Raoult’s law
Introduction to phase equilibrium
Entropy Contributions by: John L. Falconer & Will Medlin Department of Chemical and Biological Engineering University of Colorado Boulder, CO
Vapor Pressure. Evaporation u When fastest particles in a sample of liquid escape from the surface of the liquid u During evaporation the slower particles.
Phase Diagrams & Heating Curves
Noorulnajwa Diyana Yaacob PPK Bioproses Universiti Malaysia Perlis MULTIPHASE SYSTEM.
Reversible & Irreversible Processes
Classical Thermodynamics of Solutions
State Functions Contributions by: John L. Falconer & Will Medlin Department of Chemical and Biological Engineering University of Colorado Boulder, CO
SAL COLLEGE OF ENGINEERING Department of Chemical Engineering ALA CHEMICAL ENGINEERING THERMODYNAMICS -II ( ) TOPIC : SIMPLE MODELS FOR VAPOUR/LIQUID.
FRACTIONAL DISTILLATION L.E. College, Morbi Chemical Engineering Prepared by: Mehul Patel ( ) Sub: Organic Chemistry and Unit Process ( )
Chapter 14: Phase Equilibria Applications Part II.
 A. The air pressure is lower  B. The volume is lower  C. The volume is higher  D. The air pressure is higher.
Solution of Thermodynamics: Theory and applications
Liquid-Liquid Phase Equilibrium
Hemin Hasary MSc. Pharmaceutical sciences
Chapter 12 Gas-Liquid Equilibrium
The effect of applied pressure on vapor pressure
Department of Chemical Engineering, University of Nizwa
Presentation transcript:

Partially Miscible & Immiscible Solutions Contributions by: John L. Falconer & Will Medlin Department of Chemical and Biological Engineering University of Colorado Boulder, CO Supported by the National Science Foundation

Point 1 on the VLE curve represents a liquid (  ) that is enriched in component 1. What do points 2, 3, and 4 represent? A.Two liquids, L(  ) + V, two liquids B.Two liquids, L(  ) & V, liquid  C.Miscible liquid, V & L, liquid  Pressure x 1, y

Point 1 on the VLE curve represents a liquid (  ) that is enriched in component 1. What does point 5 not represent? A.Liquids  &  B.Liquids  &  and vapor C.Liquid  and vapor D.Liquid  and vapor E.Represents all of these Pressure x 1, y

Point 1 on the VLE curve represents a liquid (  ) that is enriched in component 1. Point 5 could represent _______. A.Liquids  &  B.Liquid  & vapor C.Two liquids and vapor D.None of these Pressure x 1, y

Point 1 on the VLE curve represents a liquid (  ) that is enriched in component 1. Point 6 could represent _______. A.Liquids  & , and vapor B.Two liquids C.Two vapors and liquid  D.None of these Pressure x 1, y

The equilibrium state for the B/H 2 O system at 25°C: 1)An aqueous phase with x B = )An organic phase with x H 2 O = What is the activity of B in the aqueous phase? A.Cannot determine without activity coefficients B C.1.0 D B phase H 2 O phase

A piston-cylinder contains 1 mol n-hexane (C 6 ) in VLE. At 70°C and 1 bar, 2 mol H 2 O (l) is added while temperature and pressure are held constant. What is the equilibrium state of the system? (Note: H 2 O and C 6 are immiscible) A.All vapor B.All liquid (2 liquids) C.Liquid C 6 and H 2 O, and C 6 in vapor D.Liquid H 2 O, and C 6 and H 2 O in vapor E.Liquid C, and H 2 O and C 6 in gas phase

A piston-cylinder contains 2 mol n-hexane (C 6 ) in VLE. At 70°C and 1 bar, 0.2 mol H 2 O (l) is added while temperature and pressure are held constant. What is the equilibrium state of the system? (Note: H 2 O and C 6 are immiscible) A.All vapor B.All liquid (2 liquids) C.Liquid C 6 and H 2 O, and C 6 in vapor D.Liquid H 2 O, and C 6 and H 2 O in vapor E.Liquid C, and H 2 O and C 6 in gas phase

A fixed volume container has1 mol n-C 6 (hexane) in VLE. At 60°C and 1 bar, 0.2 mol H 2 O (l) is added. What is the equilibrium state of the system at 60°C ? (Note: H 2 O and n-C 6 are immiscible) A.All vapor B.All liquid (2 liquids) C.Liquid n-C 6, and n-C 6 & H 2 O in vapor D.Liquid H 2 O and n-C 6, and n-C 6 and H 2 O in vapor Hexane 0.2 mol H 2 O (l)

A fixed volume container has1 mol n-C 6 (hexane) in VLE. At 60°C and 1 bar, 0.2 mol H 2 O (l) is added. What is the equilibrium state of the system at 60°C ? (Note: H 2 O and n-C 6 are immiscible) A.All vapor B.All liquid (2 liquids) C.Liquid n-C 6, and n-C 6 & H 2 O in vapor D.Liquid H 2 O and n-C 6, and n-C 6 and H 2 O in vapor Hexane 0.2 mol H 2 O (l)

Two components are in the vapor phase. You raise the pressure and one component condenses. What can you conclude? A.The liquids are immiscible B.The liquid that condensed had the lower vapor pressure C.The liquid that condensed had the higher vapor pressure

6 mol of A and 4 mol of B are in equilibrium at 100°C and 3 bar. A and B are completely immiscible in the liquid phase. Their vapor pressures at 100°C are: What phases are present? A.Liquid B and vapor of A + B B.Two liquids C.Two liquids in equilibrium with vapor D.All vapor E.Liquid A and vapor of A + B P B sat = 0.5 bar P A sat = 2.0 bar

6 mol of A and 4 mol of B are in equilibrium at 100°C and 2 bar. A and B are completely immiscible in the liquid phase. Their vapor pressures at 100°C are: What phases are present? A.Liquid B and vapor of A + B B.Two liquids C.Two liquids in equilibrium with vapor D.All vapor E.Liquid A and vapor of A + B P B sat = 0.5 bar P A sat = 2.0 bar

A gas phase mixture at 100°C is 75% A and 25% B. As pressure increases isothermally, liquid A starts to condense at 1.6 bar. At 2.4 bar, liquid B starts to condense. What are the vapor pressures of A and B? A.P A sat = 1.6 bar, P B sat = 2.4 bar B.P A sat = 1.2 bar, P B sat = 1.6 bar C.P A sat = 1.6 bar, P B sat = 1.2 bar D.P A sat = 1.8 bar, P B sat = 0.6 bar E.P A sat = 1.2 bar, P B sat = 1.2 bar

A gas phase mixture at 120°C is 60% A and 40% B. As pressure increases isothermally, liquid A starts to condense at 1.5 bar. At 3.0 bar, liquid B starts to condense. What are the vapor pressures of A and B? A.P A sat = 1.5 bar, P B sat = 3.0 bar B.P A sat = 1.5 bar, P B sat = 1.5 bar C.P A sat = 0.9 bar, P B sat = 3.0 bar D.P A sat = 0.9 bar, P B sat = 2.1 bar E.P A sat = 1.8 bar, P B sat = 0.6 bar

A binary gas mixture of A and B has y A = 0.6. When the pressure of this gas is raised to 2.0 bar, component A condenses, but component B does not. Which statement is correct? A.P A sat = 1.2 bar, P B sat = 0.8 bar B.P A sat = 1.2 bar, P B sat = 2.0 bar C.P A sat = 1.2 bar, P B sat > 0.8 bar D.P A sat = 2.0 bar, P B sat > 0.8 bar E.P A sat = 2.0 bar, P B sat = 0.8 bar

Liquids A and B are completely immiscible. The saturation pressure at 70°C is 0.8 bar for A and 0.6 bar for B. What partial pressures of the vapor will have a dew point at 70°C at 1.0 bar? A.P A = 0.8 bar, P B =0.2 bar B.P A = 0.5 bar, P B =0.5 bar C.P A = 0.4 bar, P B =0.6 bar D.Both A and B E.Both A and C

Liquids A and B are completely immiscible. The saturation pressure at 70°C is 0.8 bar for A and 0.6 bar for B. What composition(s) of vapor will have a dew point at 70°C at 1.0 bar? A.y A = 0.8 B.y A = 0.5 C.y A = 0.4 D.y A = 0.4 & y A = 0.8 E.y A = 0.5 & y A = 0.8

Liquids A and B are completely immiscible. The saturation pressure at 70°C for A is 0.8 bar and for B is 0.6 bar. Pressure = 1.0 bar. What composition(s) of vapor will have a dew point at 70°C? A.P A = 0.8 bar, P B = 0.2 bar B.P A = 0.5 bar, P B = 0.5 bar C.P A = 0.4 bar, P B = 0.6 bar D.Both A and C E.None of the above