Chapter 9: Phase Diagrams ISSUES to ADDRESS

Total Page:16

File Type:pdf, Size:1020Kb

Chapter 9: Phase Diagrams ISSUES to ADDRESS Chapter 9: Phase Diagrams ISSUES TO ADDRESS... • When we combine two elements... what equilibrium state do we get? • In particular, if we specify... --a composition (e.g., wt% Cu - wt% Ni), and --a temperature ( T) then... How many phases do we get? What is the composition of each phase? How much of each phase do we get? Phase A Phase B Nickel atom Copper atom Chapter 9 - 1 Phase Equilibria: Solubility Limit Introduction – Solutions – solid solutions, single phase – Mixtures – more than one phase Adapted from Fig. 9.1, Callister 7e. Sucrose/Water Phase Diagram • Solubility Limit : 100 Max concentration for Solubility which only a single phase 80 Limit L solution occurs. (liquid) 60 L + Question: What is the 40 (liquid solution S solubility limit at 20°C? i.e., syrup) (solid 20 Temperature (°C) Temperature sugar) Answer: 65 wt% sugar . If C < 65 wt% sugar: syrup o 0 20 40 60 65 80 100 If Co > 65 wt% sugar: syrup + sugar. Co =Composition (wt% sugar) Sugar Pure Pure Water Chapter 9 - 2 Components and Phases • Components : The elements or compounds which are present in the mixture (e.g., Al and Cu) • Phases : The physically and chemically distinct material regions that result (e.g., α and β). Aluminum- β (lighter Copper phase) Alloy α (darker phase) Adapted from chapter-opening photograph, Chapter 9, Callister 3e. A phase maybe defined as a homogeneous portion of a system that has Chapter 9 - 3 uniform physical and chemical characteristics. Effect of T & Composition ( Co) • Changing T can change # of phases: path A to B. • Changing Co can change # of phases: path B to D. B (100°C,70) D (100°C,90) 1 phase 2 phases 100 80 L (liquid) water- 60 + sugar L S (liquid solution system 40 (solid i.e., syrup) sugar) 20 A (20°C,70) Temperature (°C) 2 phases Adapted from 0 Fig. 9.1, 0 20 40 60 7080 100 Callister 7e. Co =Composition (wt% sugar) Chapter 9 - 4 Phase Equilibrium Equilibrium: minimum energy state for a given T, P, and composition (i.e. equilibrium state will persist indefinitely for a fixed T, P and composition). Phase Equilibrium: If there is more than 1 phase present, phase characteristics will stay constant over time. Phase diagrams tell us about equilibrium phases as a function of T, P and composition (here, we’ll always keep P constant for simplicity). Chapter 9 - 5 Unary Systems Triple point Chapter 9 - 6 Phase Equilibria Simple solution system (e.g., Ni-Cu solution) Crystal electroneg r (nm) Structure Ni FCC 1.9 0.1246 Cu FCC 1.8 0.1278 • Both have the same crystal structure (FCC) and have similar electronegativities and atomic radii ( W. Hume – Rothery rules ) suggesting high mutual solubility. • Ni and Cu are totally miscible in all proportions. Chapter 9 - 7 Unary Systems Single component system Consider 2 metals: Cu has melting T = 1085 oC Ni has melting T = 1453 oC (at standard P = 1 atm) T T liquid liquid 1453 oC 1085 oC solid solid Cu Ni Chapter 9 - 8 What happens when Cu and Ni are mixed? Binary Isomorphous Systems 2 components Complete liquid and solid solubility Expect T m of solution to lie in between T m of two pure components T T For a pure liquid component, complete melting occurs before T liquid L 1453 oC increases (sharp phase transition). But for 1085 oC multicomponent solid systems, there is S solid usually a coexistence of L 0 100 and S. Cu wt% Ni Ni Chapter 9 - 9 Phase Diagrams • Indicate phases as function of T, Co, and P. • For this course: -binary systems: just 2 components. -independent variables: T and Co (P = 1 atm is almost always used). T(°C) 1600 • 2 phases: • Phase L (liquid) Diagram 1500 for Cu-Ni L (liquid) α (FCC solid solution) system 1400 • 3 phase fields: s du L ui α 1300 liq + us L + α L id ol 1200 s α α Adapted from Fig. 9.3(a), Callister 7e. (Fig. 9.3(a) is adapted from Phase 1100 (FCC solid Diagrams of Binary Nickel Alloys , P. Nash (Ed.), ASM International, Materials Park, solution) OH (1991). 1000 0 20 40 60 80 100 wt% Ni Chapter 9 - 10 Phase Diagrams : # and types of phases • Rule 1: If we know T and Co, then we know: --the # and types of phases present. T(°C) • Examples: 1600 A(1100°C, 60): L (liquid) 1500 1 phase: α s Cu-Ni du ui iq phase B(1250°C, 35): 1400 l us lid 2 phases: L + α so diagram (1250°C,35) α 1300 + α B L (FCC solid 1200 solution) Adapted from Fig. 9.3(a), Callister 7e. (Fig. 9.3(a) is adapted from Phase 1100 A(1100°C,60) Diagrams of Binary Nickel Alloys , P. Nash (Ed.), ASM International, Materials Park, OH, 1991). 1000 0 20 40 60 80 100 wt% Ni Chapter 9 - 11 Phase Diagrams : composition of phases • Rule 2: If we know T and Co, then we know: --the composition of each phase. Cu-Ni system • Examples: T(°C) A C = 35 wt% Ni T tie line s o A idu iqu At TA = 1320°C: 1300 L (liquid) l + α Only Liquid ( L) L B us T olid CL = C o ( = 35 wt% Ni) B s α At TD = 1190°C: + α 1200 L D (solid) Only Solid ( α) TD Cα = Co ( = 35 wt% Ni ) 20 3032 35 4043 50 At TB = 1250°C: CLCo Cα wt% Ni Both α and L Adapted from Fig. 9.3(b), Callister 7e. (Fig. 9.3(b) is adapted from Phase Diagrams CL = Cliquidus ( = 32 wt% Ni here) of Binary Nickel Alloys , P. Nash (Ed.), ASM Cα = Csolidus ( = 43 wt% Ni here) International, Materials Park, OH, 1991.) Chapter 9 - 12 Determining phase composition in 2-phase region: 1. Draw the tie line. 2. Note where the tie line intersects the liquidus and solidus lines (i.e. where the tie line crosses the phase boundaries). 3. Read off the composition at the boundaries: Liquid is composed of CL amount of Ni (31.5 wt% Ni). Solid is composed of Cααα amount of Ni (42.5 wt% Ni). Chapter 9 - 13 Phase Diagrams : weight fractions of phases • Rule 3: If we know T and Co, then we know: --the amount of each phase (given in wt%). Cu-Ni • Examples: T(°C) system Co = 35 wt% Ni T A A tie line dus qui At TA: Only Liquid (L) 1300 L (liquid) li α W = 100 wt%, W = 0 L + L α B s idu At TD: Only Solid ( α) TB R S sol α WL = 0, Wα = 100 wt% + α 1200 L D (solid) At TB: Both α and L TD S 43 − 35 20 30 40 50 W = = = 73 wt % 32 35 43 L R +S 43 − 32 CLCo Cα wt% Ni Adapted from Fig. 9.3(b), Callister 7e. R (Fig. 9.3(b) is adapted from Phase Diagrams of Wα = = 27 wt% Binary Nickel Alloys , P. Nash (Ed.), ASM R +S International, Materials Park, OH, 1991.) Chapter 9 - 14 Lever Rule: Derivation Since we have only 2 phases: W W (1) L + α =1 Conservation of mass requires that: Amount of Ni in α-phase + amount of Ni in liquid phase = total amount of Ni or W C W C C (2) α α + L L = o From 1 st condition, we have: W W α =1− L W C W C C Sub-in to (2): 1( − L ) α + L L = o W W Solving for L and α gives : C − C C − C W = α o W = o L L C C α C C α − L α − L Chapter 9 - 15 The Lever Rule • Tie line – connects the phases in equilibrium with each other - essentially an isotherm T(°C) How much of each phase? tie line dus qui Think of it as a lever (teeter-totter) 1300 L (liquid) li + α M M L L α B s idu TB sol α + α 1200 L (solid) R S R S 20 30CL C 40C 50 o ααα M α ⋅S = M L ⋅R wt% Ni Adapted from Fig. 9.3(b), Callister 7e. ML S Cα −C0 R C0 −CL WL = = = Wα = = ML + Mα R + S Cα −CL R + S Cα −CL Chapter 9 - 16 Ex: Cooling in a Cu-Ni Binary • Phase diagram: T(°C) L (liquid) L: 35wt%Ni Cu-Ni system. Cu-Ni system • System is: 1300 α A + -- binary L: 35 wt% Ni L α: 46 wt% Ni B i.e. , 2 components: 35 46 32 C Cu and Ni. 43 -- isomorphous D 24 36 L: 32 wt% Ni i.e., complete α α: 43 wt% Ni 1200 + solubility of one L E component in L: 24 wt% Ni another; α phase α α: 36 wt% Ni field extends from (solid) 0 to 100 wt% Ni. • Consider 1100 Co = 35 wt%Ni . 20 3035 40 50 Adapted from Fig. 9.4, Co wt% Ni Callister 7e. Chapter 9 - 17 Microstructures in Isomorphous Alloys Microstructures will vary on the cooling rate (i.e. processing conditions) 1. Equilibrium Cooling: Very slow cooling to allow phase equilibrium to be maintained during the cooling process. a (T>1260 oC): start as homogeneous liquid solution. b (T ~ 1260 oC): liquidus line reached. α phase begins to nucleate. Cα = 46 wt% Ni; C L = 35 wt% Ni c (T= 1250 oC): calculate composition and mass fraction of each phase. Cα = 43 wt% Ni; CL = 32 wt% Ni d (T~ 1220 oC): solidus line reached.
Recommended publications
  • Thermodynamics
    TREATISE ON THERMODYNAMICS BY DR. MAX PLANCK PROFESSOR OF THEORETICAL PHYSICS IN THE UNIVERSITY OF BERLIN TRANSLATED WITH THE AUTHOR'S SANCTION BY ALEXANDER OGG, M.A., B.Sc., PH.D., F.INST.P. PROFESSOR OF PHYSICS, UNIVERSITY OF CAPETOWN, SOUTH AFRICA THIRD EDITION TRANSLATED FROM THE SEVENTH GERMAN EDITION DOVER PUBLICATIONS, INC. FROM THE PREFACE TO THE FIRST EDITION. THE oft-repeated requests either to publish my collected papers on Thermodynamics, or to work them up into a comprehensive treatise, first suggested the writing of this book. Although the first plan would have been the simpler, especially as I found no occasion to make any important changes in the line of thought of my original papers, yet I decided to rewrite the whole subject-matter, with the inten- tion of giving at greater length, and with more detail, certain general considerations and demonstrations too concisely expressed in these papers. My chief reason, however, was that an opportunity was thus offered of presenting the entire field of Thermodynamics from a uniform point of view. This, to be sure, deprives the work of the character of an original contribution to science, and stamps it rather as an introductory text-book on Thermodynamics for students who have taken elementary courses in Physics and Chemistry, and are familiar with the elements of the Differential and Integral Calculus. The numerical values in the examples, which have been worked as applications of the theory, have, almost all of them, been taken from the original papers; only a few, that have been determined by frequent measurement, have been " taken from the tables in Kohlrausch's Leitfaden der prak- tischen Physik." It should be emphasized, however, that the numbers used, notwithstanding the care taken, have not vii x PREFACE.
    [Show full text]
  • Recent Progress on Deep Eutectic Solvents in Biocatalysis Pei Xu1,2, Gao‑Wei Zheng3, Min‑Hua Zong1,2, Ning Li1 and Wen‑Yong Lou1,2*
    Xu et al. Bioresour. Bioprocess. (2017) 4:34 DOI 10.1186/s40643-017-0165-5 REVIEW Open Access Recent progress on deep eutectic solvents in biocatalysis Pei Xu1,2, Gao‑Wei Zheng3, Min‑Hua Zong1,2, Ning Li1 and Wen‑Yong Lou1,2* Abstract Deep eutectic solvents (DESs) are eutectic mixtures of salts and hydrogen bond donors with melting points low enough to be used as solvents. DESs have proved to be a good alternative to traditional organic solvents and ionic liq‑ uids (ILs) in many biocatalytic processes. Apart from the benign characteristics similar to those of ILs (e.g., low volatil‑ ity, low infammability and low melting point), DESs have their unique merits of easy preparation and low cost owing to their renewable and available raw materials. To better apply such solvents in green and sustainable chemistry, this review frstly describes some basic properties, mainly the toxicity and biodegradability of DESs. Secondly, it presents several valuable applications of DES as solvent/co-solvent in biocatalytic reactions, such as lipase-catalyzed transester‑ ifcation and ester hydrolysis reactions. The roles, serving as extractive reagent for an enzymatic product and pretreat‑ ment solvent of enzymatic biomass hydrolysis, are also discussed. Further understanding how DESs afect biocatalytic reaction will facilitate the design of novel solvents and contribute to the discovery of new reactions in these solvents. Keywords: Deep eutectic solvents, Biocatalysis, Catalysts, Biodegradability, Infuence Introduction (1998), one concept is “Safer Solvents and Auxiliaries”. Biocatalysis, defned as reactions catalyzed by bio- Solvents represent a permanent challenge for green and catalysts such as isolated enzymes and whole cells, has sustainable chemistry due to their vast majority of mass experienced signifcant progress in the felds of either used in catalytic processes (Anastas and Eghbali 2010).
    [Show full text]
  • Lecture 15: 11.02.05 Phase Changes and Phase Diagrams of Single- Component Materials
    3.012 Fundamentals of Materials Science Fall 2005 Lecture 15: 11.02.05 Phase changes and phase diagrams of single- component materials Figure removed for copyright reasons. Source: Abstract of Wang, Xiaofei, Sandro Scandolo, and Roberto Car. "Carbon Phase Diagram from Ab Initio Molecular Dynamics." Physical Review Letters 95 (2005): 185701. Today: LAST TIME .........................................................................................................................................................................................2� BEHAVIOR OF THE CHEMICAL POTENTIAL/MOLAR FREE ENERGY IN SINGLE-COMPONENT MATERIALS........................................4� The free energy at phase transitions...........................................................................................................................................4� PHASES AND PHASE DIAGRAMS SINGLE-COMPONENT MATERIALS .................................................................................................6� Phases of single-component materials .......................................................................................................................................6� Phase diagrams of single-component materials ........................................................................................................................6� The Gibbs Phase Rule..................................................................................................................................................................7� Constraints on the shape of
    [Show full text]
  • Phase Diagrams
    Module-07 Phase Diagrams Contents 1) Equilibrium phase diagrams, Particle strengthening by precipitation and precipitation reactions 2) Kinetics of nucleation and growth 3) The iron-carbon system, phase transformations 4) Transformation rate effects and TTT diagrams, Microstructure and property changes in iron- carbon system Mixtures – Solutions – Phases Almost all materials have more than one phase in them. Thus engineering materials attain their special properties. Macroscopic basic unit of a material is called component. It refers to a independent chemical species. The components of a system may be elements, ions or compounds. A phase can be defined as a homogeneous portion of a system that has uniform physical and chemical characteristics i.e. it is a physically distinct from other phases, chemically homogeneous and mechanically separable portion of a system. A component can exist in many phases. E.g.: Water exists as ice, liquid water, and water vapor. Carbon exists as graphite and diamond. Mixtures – Solutions – Phases (contd…) When two phases are present in a system, it is not necessary that there be a difference in both physical and chemical properties; a disparity in one or the other set of properties is sufficient. A solution (liquid or solid) is phase with more than one component; a mixture is a material with more than one phase. Solute (minor component of two in a solution) does not change the structural pattern of the solvent, and the composition of any solution can be varied. In mixtures, there are different phases, each with its own atomic arrangement. It is possible to have a mixture of two different solutions! Gibbs phase rule In a system under a set of conditions, number of phases (P) exist can be related to the number of components (C) and degrees of freedom (F) by Gibbs phase rule.
    [Show full text]
  • Phase Transitions in Multicomponent Systems
    Physics 127b: Statistical Mechanics Phase Transitions in Multicomponent Systems The Gibbs Phase Rule Consider a system with n components (different types of molecules) with r phases in equilibrium. The state of each phase is defined by P,T and then (n − 1) concentration variables in each phase. The phase equilibrium at given P,T is defined by the equality of n chemical potentials between the r phases. Thus there are n(r − 1) constraints on (n − 1)r + 2 variables. This gives the Gibbs phase rule for the number of degrees of freedom f f = 2 + n − r A Simple Model of a Binary Mixture Consider a condensed phase (liquid or solid). As an estimate of the coordination number (number of nearest neighbors) think of a cubic arrangement in d dimensions giving a coordination number 2d. Suppose there are a total of N molecules, with fraction xB of type B and xA = 1 − xB of type A. In the mixture we assume a completely random arrangement of A and B. We just consider “bond” contributions to the internal energy U, given by εAA for A − A nearest neighbors, εBB for B − B nearest neighbors, and εAB for A − B nearest neighbors. We neglect other contributions to the internal energy (or suppose them unchanged between phases, etc.). Simple counting gives the internal energy of the mixture 2 2 U = Nd(xAεAA + 2xAxBεAB + xBεBB) = Nd{εAA(1 − xB) + εBBxB + [εAB − (εAA + εBB)/2]2xB(1 − xB)} The first two terms in the second expression are just the internal energy of the unmixed A and B, and so the second term, depending on εmix = εAB − (εAA + εBB)/2 can be though of as the energy of mixing.
    [Show full text]
  • Introduction to Phase Diagrams*
    ASM Handbook, Volume 3, Alloy Phase Diagrams Copyright # 2016 ASM InternationalW H. Okamoto, M.E. Schlesinger and E.M. Mueller, editors All rights reserved asminternational.org Introduction to Phase Diagrams* IN MATERIALS SCIENCE, a phase is a a system with varying composition of two com- Nevertheless, phase diagrams are instrumental physically homogeneous state of matter with a ponents. While other extensive and intensive in predicting phase transformations and their given chemical composition and arrangement properties influence the phase structure, materi- resulting microstructures. True equilibrium is, of atoms. The simplest examples are the three als scientists typically hold these properties con- of course, rarely attained by metals and alloys states of matter (solid, liquid, or gas) of a pure stant for practical ease of use and interpretation. in the course of ordinary manufacture and appli- element. The solid, liquid, and gas states of a Phase diagrams are usually constructed with a cation. Rates of heating and cooling are usually pure element obviously have the same chemical constant pressure of one atmosphere. too fast, times of heat treatment too short, and composition, but each phase is obviously distinct Phase diagrams are useful graphical representa- phase changes too sluggish for the ultimate equi- physically due to differences in the bonding and tions that show the phases in equilibrium present librium state to be reached. However, any change arrangement of atoms. in the system at various specified compositions, that does occur must constitute an adjustment Some pure elements (such as iron and tita- temperatures, and pressures. It should be recog- toward equilibrium. Hence, the direction of nium) are also allotropic, which means that the nized that phase diagrams represent equilibrium change can be ascertained from the phase dia- crystal structure of the solid phase changes with conditions for an alloy, which means that very gram, and a wealth of experience is available to temperature and pressure.
    [Show full text]
  • Phase Diagrams of Ternary -Conjugated Polymer Solutions For
    polymers Article Phase Diagrams of Ternary π-Conjugated Polymer Solutions for Organic Photovoltaics Jung Yong Kim School of Chemical Engineering and Materials Science and Engineering, Jimma Institute of Technology, Jimma University, Post Office Box 378 Jimma, Ethiopia; [email protected] Abstract: Phase diagrams of ternary conjugated polymer solutions were constructed based on Flory-Huggins lattice theory with a constant interaction parameter. For this purpose, the poly(3- hexylthiophene-2,5-diyl) (P3HT) solution as a model system was investigated as a function of temperature, molecular weight (or chain length), solvent species, processing additives, and electron- accepting small molecules. Then, other high-performance conjugated polymers such as PTB7 and PffBT4T-2OD were also studied in the same vein of demixing processes. Herein, the liquid-liquid phase transition is processed through the nucleation and growth of the metastable phase or the spontaneous spinodal decomposition of the unstable phase. Resultantly, the versatile binodal, spinodal, tie line, and critical point were calculated depending on the Flory-Huggins interaction parameter as well as the relative molar volume of each component. These findings may pave the way to rationally understand the phase behavior of solvent-polymer-fullerene (or nonfullerene) systems at the interface of organic photovoltaics and molecular thermodynamics. Keywords: conjugated polymer; phase diagram; ternary; polymer solutions; polymer blends; Flory- Huggins theory; polymer solar cells; organic photovoltaics; organic electronics Citation: Kim, J.Y. Phase Diagrams of Ternary π-Conjugated Polymer 1. Introduction Solutions for Organic Photovoltaics. Polymers 2021, 13, 983. https:// Since Flory-Huggins lattice theory was conceived in 1942, it has been widely used be- doi.org/10.3390/polym13060983 cause of its capability of capturing the phase behavior of polymer solutions and blends [1–3].
    [Show full text]
  • Section 1 Introduction to Alloy Phase Diagrams
    Copyright © 1992 ASM International® ASM Handbook, Volume 3: Alloy Phase Diagrams All rights reserved. Hugh Baker, editor, p 1.1-1.29 www.asminternational.org Section 1 Introduction to Alloy Phase Diagrams Hugh Baker, Editor ALLOY PHASE DIAGRAMS are useful to exhaust system). Phase diagrams also are con- terms "phase" and "phase field" is seldom made, metallurgists, materials engineers, and materials sulted when attacking service problems such as and all materials having the same phase name are scientists in four major areas: (1) development of pitting and intergranular corrosion, hydrogen referred to as the same phase. new alloys for specific applications, (2) fabrica- damage, and hot corrosion. Equilibrium. There are three types of equili- tion of these alloys into useful configurations, (3) In a majority of the more widely used commer- bria: stable, metastable, and unstable. These three design and control of heat treatment procedures cial alloys, the allowable composition range en- conditions are illustrated in a mechanical sense in for specific alloys that will produce the required compasses only a small portion of the relevant Fig. l. Stable equilibrium exists when the object mechanical, physical, and chemical properties, phase diagram. The nonequilibrium conditions is in its lowest energy condition; metastable equi- and (4) solving problems that arise with specific that are usually encountered inpractice, however, librium exists when additional energy must be alloys in their performance in commercial appli- necessitate the knowledge of a much greater por- introduced before the object can reach true stabil- cations, thus improving product predictability. In tion of the diagram. Therefore, a thorough under- ity; unstable equilibrium exists when no addi- all these areas, the use of phase diagrams allows standing of alloy phase diagrams in general and tional energy is needed before reaching meta- research, development, and production to be done their practical use will prove to be of great help stability or stability.
    [Show full text]
  • Chapter 10 Gibbs Free Energy Composition and Phase Diagrams of Binary Systems 10.2 Gibbs Free Energy and Thermodynamic Activity
    Chapter 10 Gibbs Free Energy Composition and Phase Diagrams of Binary Systems 10.2 Gibbs Free Energy and Thermodynamic Activity The Gibbs free energy of mixing of the components A and B to form a mole of solution: If it is ideal, i.e., if ai=Xi, then the molar Gibbs free energy of mixing, Figure 10.1 The molar Gibbs free energies of Figure 10.2 The activities of component B mixing in binary systems exhibiting ideal behavior obtained from lines I, II, and III in Fig. 10.1. (I), positive deviation from ideal behavior (II), and negative deviation from ideal behavior (III). 10.3 The Gibbs Free Energy of Formation of Regular Solutions If curves II and III for regular solutions, then deviation of from , is ∆ ∆ For curve II, < , , and thus is a positive quantity ( and Ω are positive quantities). ∆ ∆ ∆ Figure 10.3 The effect of the magnitude of a on the integral molar heats and integral molar Gibbs free energies of formation of a binary regular solution. 10.3 The Gibbs Free Energy of Formation of Regular Solutions The equilibrium coexistence of two separate solutions at the temperature T and pressure P requires that and Subtracting from both sides of Eq. (i) gives 0 or Similarly Figure 10.4 (a) The molar Gibbs free energies of mixing of binary components which form a complete range of solutions. (b) The molar Gibbs free energies of mixing of binary components in a system which exhibits a miscibility gap. 10.4 Criteria for Phase Stability in Regular Solutions For a regular solution, and 3 3 At XA=XB=0.5, the third derivative, / XB =0, 2 2 and thus the second derivative, / XB =0 at XA=0.5 ∆ When α=2 ⇒ the critical value of ∆αabove which phase separation occurs.
    [Show full text]
  • Lecture 36. the Phase Rule
    Lecture 36. The Phase Rule P = number of phases C = number of components (chemically independent constituents) F = number of degrees of freedom xC,P = the mole fraction of component C in phase P The variables used to describe a system in equilibrium: x11, x21, x31,...,xC −1,1 phase 1 x12 , x22 , x32 ,..., xC−1,2 phase 2 x1P , x2P , x3P ,...,xC−1,P phase P T,P Total number of variables = P(C-1) + 2 Constraints on the system: m11 = m12 = m13 =…= m1,P P - 1 relations m21 = m22 = m23 =…= m2,P P - 1 relations mC,1 = mC,2 = mC,3 =…= mC,P P - 1 relations 1 Total number of constraints = C(P - 1) Degrees of freedom = variables - constraints F=P(C- 1) + 2 - C(P - 1) F=C- P+2 Single Component Systems: F = 3 - P In single phase regions, F = 2. Both T and P may vary. At the equilibrium between two phases, F = 1. Changing T requires a change in P, and vice versa. At the triple point, F = 0. Tt and Pt are unique. 2 Four phases cannot be in equilibrium (for a single component.) Two Component Systems: F = 4 - P The possible phases are the vapor, two immiscible (or partially miscible) liquid phases, and two solid phases. (Of course, they don’t have to all exist. The liquids might turn out to be miscible for all compositions.) 3 Liquid-Vapor Equilibrium Possible degrees of freedom: T, P, mole fraction of A xA = mole fraction of A in the liquid yA = mole fraction of A in the vapor zA = overall mole fraction of A (for the entire system) We can plot either T vs zA holding P constant, or P vs zA holding T constant.
    [Show full text]
  • Continuous Eutectic Freeze Crystallisation
    CONTINUOUS EUTECTIC FREEZE CRYSTALLISATION Report to the Water Research Commission by Jemitias Chivavava, Benita Aspeling, Debbie Jooste, Edward Peters, Dereck Ndoro, Hilton Heydenrych, Marcos Rodriguez Pascual and Alison Lewis Crystallisation and Precipitation Research Unit Department of Chemical Engineering University of Cape Town WRC Report No. 2229/1/18 ISBN 978-1-4312-0996-5 July 2018 Obtainable from Water Research Commission Private Bag X03 Gezina, 0031 [email protected] or download from www.wrc.org.za DISCLAIMER This report has been reviewed by the Water Research Commission (WRC) and approved for publication. Approval does not signify that the contents necessarily reflect the views and policies of the WRC nor does mention of trade names or commercial products constitute endorsement or recommendation for use. Printed in the Republic of South Africa © Water Research Commission ii Executive summary Eutectic Freeze Crystallisation (EFC) has shown great potential to treat industrial brines with the benefits of recovering potentially valuable salts and very pure water. So far, many studies that have been concerned with the development of EFC have all been carried out (1) in batch mode and (2) have not considered the effect of minor components that may affect the process efficiency and product quality. Brines generated in industrial operations often contain antiscalants that are dosed in cooling water and reverse osmosis feed streams to prevent scaling of heat exchangers and membrane fouling. These antiscalants may affect the EFC process, especially the formation of salts. The first aim of this work was to understand the effects of antiscalants on thermodynamics and crystallisation kinetics in EFC.
    [Show full text]
  • VAPOR-LIQUID EQUILIBRIA Using the Gibbs Energy and the Common Tangent Plane Criterion
    ChE curriculum VAPOR-LIQUID EQUILIBRIA Using the Gibbs Energy and the Common Tangent Plane Criterion MARÍA DEL MAR OLAYA, JUAN A. REYES-LABARTA, MARÍA DOLORES SERRANO, ANTONIO MARCILLA University of Alicante • Apdo. 99, Alicante 03080, Spain hase thermodynamics is often perceived as a difficult overall composition. This is the case with the binary system subject with which many students never become fully in Figure 1(a); it is homogeneous for all compositions. The gM comfortable. It is our opinion that the Gibbsian geo- vs. composition curve is concave down, meaning that no split Pmetrical framework, which can be easily represented in Excel occurs in the global mixture composition to give two liquid spreadsheets, can help students to gain a better understanding phases. Geometrically, this implies that it is impossible to find of phase equilibria using only elementary concepts of high two different points on the gM curve sharing a common tangent school geometry. line. In contrast, the change of curvature in the gM function Phase equilibrium calculations are essential to the simula- as shown in Figure 1(b) permits the existence of two conju- tion and optimization of chemical processes. The task with gated points (I and II) that do share a common tangent line these calculations is to accurately predict the correct number and which, in turn, lead to the formation of two equilibrium of phases at equilibrium present in the system and their com- liquid phases (LL). Any initial mixture, as for example zi in positions. Methods for these calculations can be divided into Figure 1(b), located between the inflection points s on the M 2 M dx2 two main categories: the equation-solving approach (K-value g curve, is intrinsically unstable (d g / i <0) and splits method) and minimization of the Gibbs free energy.
    [Show full text]