Docsity
Docsity

Prepare for your exams
Prepare for your exams

Study with the several resources on Docsity


Earn points to download
Earn points to download

Earn points by helping other students or get them with a premium plan


Guidelines and tips
Guidelines and tips

Solution Thermodynamics - Chemical Engineering Thermodynamics II, Slides of Thermodynamics

Partial molar properties, ideal and non ideal solutions, standard state, Gibbs-Duhem equation are important subtopic in this lecture

Typology: Slides

2020/2021

Uploaded on 06/21/2021

ekanaaa
ekanaaa 🇺🇸

4.3

(28)

268 documents

1 / 81

Toggle sidebar

This page cannot be seen from the preview

Don't miss anything!

bg1
Solution Thermodynamics
CH2351 Chemical Engineering Thermodynamics II
Unit – I, II
www.msubbu.in
Dr. M. Subramanian
Associate Professor
Department of Chemical Engineering
Sri Sivasubramaniya Nadar College of Engineering
Kalavakkam 603 110, Kanchipuram (Dist)
Tamil Nadu, India
msubbu.in[AT]gmail.com
Jan-2012
www.msubbu.in
pf3
pf4
pf5
pf8
pf9
pfa
pfd
pfe
pff
pf12
pf13
pf14
pf15
pf16
pf17
pf18
pf19
pf1a
pf1b
pf1c
pf1d
pf1e
pf1f
pf20
pf21
pf22
pf23
pf24
pf25
pf26
pf27
pf28
pf29
pf2a
pf2b
pf2c
pf2d
pf2e
pf2f
pf30
pf31
pf32
pf33
pf34
pf35
pf36
pf37
pf38
pf39
pf3a
pf3b
pf3c
pf3d
pf3e
pf3f
pf40
pf41
pf42
pf43
pf44
pf45
pf46
pf47
pf48
pf49
pf4a
pf4b
pf4c
pf4d
pf4e
pf4f
pf50
pf51

Partial preview of the text

Download Solution Thermodynamics - Chemical Engineering Thermodynamics II and more Slides Thermodynamics in PDF only on Docsity!

CH2351 Chemical Engineering Thermodynamics IISolution Thermodynamics

Unit – I, II

www.msubbu.in

Dr. M. Subramanian

Associate Professor

Department of Chemical Engineering

Sri Sivasubramaniya Nadar College of Engineering

Kalavakkam – 603 110, Kanchipuram (Dist)

Tamil Nadu, India msubbu.in[AT]gmail.com

www.msubbu.in

Contents

  • UNIT I: PROPERTIES OF SOLUTIONS -^

Partial molar properties, ideal and non-ideal solutions, standardstates definition and choice, Gibbs-Duhem equation, excessproperties of mixtures.

  • UNIT II:

PHASE EQUILIBRIA

-^

Criteria for equilibrium between phases in multi component non-reacting systems in terms of chemical potential and fugacity M Subramanian

Introduction

•^

Most of the materials of the real world are not pure substanceswith all atoms or molecules identical but rather are mixtures ofone type or another.

-^

The pure substances from which a solution may be prepared are called

components

, or constituents, of the solution.

called

components

, or constituents, of the solution.

•^

Solutions are not limited to liquids: for example air, a mixture ofpredominantly N

2

and O

, forms a vapor solution. Solid solutions 2

such as the solid phase in the Si-Ge system are also common M Subramanian

Multicomponent Systems – Basic Relations

  • Single component system:
    • Intensive properties: depends on Pressure, Temperature– Extensive properties: depends on Pressure, Temperature, and

amount

  • Multicomponent system:
    • Intensive properties: depends on Pressure, Temperature, and

composition

  • Extensive properties: depends on Pressure, Temperature,

amount of each component M Subramanian

Other Measures of Composition

•^

Mass fraction – preferable where the definition of molecularweight is ambiguous (eg. Polymer molecules)

-^

Molarity – moles per litre of solution

-^

Molality

moles per kilogram of solvent. The molality is usually

•^

Molality

moles per kilogram of solvent. The molality is usually

preferred, since it does not depend on temperature or pressure,whereas any concentration unit is so dependent.

-^

Volume fraction

-^

Mole ratio or volume ratio (for binary systems) M Subramanian

Properties of Solutions

•^

The properties of solutions are, in general, not additiveproperties of the pure components.

-^

The actual contribution to any extensive property is designatedas its partial property. The term partial property is used todesignate the property of a component when it is in admixture with one or more other componentswith one or more other components

-^

Because most chemical, biological, and geological processesoccur at constant temperature and pressure, it is convenient toprovide a special name for the partial derivatives of allthermodynamic properties with respect to mole number atconstant pressure and temperature. They are called

partial

molar properties M Subramanian

www.msubbu.in

M Subramanian

M Subramanian

Partial Molar Volume

•^

Benzene-Toluene:

Benzene and toluene form an ideal solution.

The volume of 1 mole pure benzene is 88.9 ml; the volume of 1mole pure toluene is 106.4 ml. 88.9 ml benzene mixed with106.4 ml toluene results in 88.9 ml + 106.4 ml, or 195.3 ml ofsolution. (

ideal solution

•^

Ethanol-Water:^ –

The volume of 1 mole pure ethanol is 58.0 ml and the volume– The volume of 1 mole pure ethanol is 58.0 ml and the volume^ of 1 mole pure water is 18.0 ml. However, 1 mole watermixed with 1 mole ethanol does not result in 58.0 ml + 18.0ml, or 76.0 ml, but rather 74.

ml.

  • When the mole fraction is 0.5, the partial molal volume of

ethanol is 57.4 ml and the partial molal volume of water is16.9 ml.

(non-ideal solution)

M Subramanian

www.msubbu.in

Fundamental Equations of Solution

Thermodynamics

M Subramanian

M Subramanian

M Subramanian