Some Thermodynamic Relations at the Critical Point in Liquid-Vapor Systems (Analyticity/Symmetry/Specific Heats/Critical Exponents/Coexistence Curve) 0
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Phase Diagrams and Phase Separation
Phase Diagrams and Phase Separation Books MF Ashby and DA Jones, Engineering Materials Vol 2, Pergamon P Haasen, Physical Metallurgy, G Strobl, The Physics of Polymers, Springer Introduction Mixing two (or more) components together can lead to new properties: Metal alloys e.g. steel, bronze, brass…. Polymers e.g. rubber toughened systems. Can either get complete mixing on the atomic/molecular level, or phase separation. Phase Diagrams allow us to map out what happens under different conditions (specifically of concentration and temperature). Free Energy of Mixing Entropy of Mixing nA atoms of A nB atoms of B AM Donald 1 Phase Diagrams Total atoms N = nA + nB Then Smix = k ln W N! = k ln nA!nb! This can be rewritten in terms of concentrations of the two types of atoms: nA/N = cA nB/N = cB and using Stirling's approximation Smix = -Nk (cAln cA + cBln cB) / kN mix S AB0.5 This is a parabolic curve. There is always a positive entropy gain on mixing (note the logarithms are negative) – so that entropic considerations alone will lead to a homogeneous mixture. The infinite slope at cA=0 and 1 means that it is very hard to remove final few impurities from a mixture. AM Donald 2 Phase Diagrams This is the situation if no molecular interactions to lead to enthalpic contribution to the free energy (this corresponds to the athermal or ideal mixing case). Enthalpic Contribution Assume a coordination number Z. Within a mean field approximation there are 2 nAA bonds of A-A type = 1/2 NcAZcA = 1/2 NZcA nBB bonds of B-B type = 1/2 NcBZcB = 1/2 NZ(1- 2 cA) and nAB bonds of A-B type = NZcA(1-cA) where the factor 1/2 comes in to avoid double counting and cB = (1-cA). -
Ionic Liquid and Supercritical Fluid Hyphenated Techniques for Dissolution and Separation of Lanthanides, Actinides, and Fission Products
Project No. 09-805 Ionic Liquid and Supercritical Fluid Hyphenated Techniques for Dissolution and Separation of Lanthanides, Actinides, and Fission Products ItIntegrat tdUied Universit itPy Programs Dr. Chien Wai University of Idaho In collaboration with: Idaho National Laboratory Jack Law, Technical POC James Bresee, Federal POC 1 Ionic Liquid and Supercritical Fluid Hyphenated Techniques For Dissolution and Separation of Lanthanides and Actinides DOE-NEUP Project (TO 00058) Final Technical Report Principal Investigator: Chien M. Wai Department of Chemistry, University of Idaho, Moscow, Idaho 83844 Date: December 1, 2012 2 Table of Contents Project Summary 3 Publications Derived from the Project 5 Chapter I. Introduction 6 Chapter II. Uranium Dioxide in Ionic Liquid with a TP-HNO3 Complex – Dissolution and Coordination Environment 9 1. Dissolution of UO2 in Ionic Liquid with TBP(HNO3)1.8(H2O)0.6 2. Raman Spectra of Dissolved Uranyl Species in IL 13 3. Transferring Uranium from IL Phase to sc-CO2 15 Chapter III. Kinetic Study on Dissolution of Uranium Dioxide and Neodymium Sesquioxide in Ionic Liquid 19 1. Rate of Dissolution of UO2 and Nd2O3 in RTIL 19 2. Temperature Effect on Dissolution of UO2 and Nd2O3 24 3. Viscosity Effect on Dissolution of UO2 in IL with TBP(HNO3)1.8(H2O)0.6 Chapter IV. Separation of UO2(NO3)2(TBP)2 and Nd(NO3)3(TBP)3 in Ionic Liquid Using Diglycolamide and Supercritical CO2 Extraction 30 1. Complexation of Uranyl with Diglycolamide TBDGA in Ionic Liquid 31 2. Complexation of Neodymium(III) with TBDGA in Ionic Liquid 35 3. Solubility and Distribution Ratio of UO2(NO3)2(TBP)2 and Nd(NO3)3(TBP)3 in Supercritical CO2 Phase 38 4. -
Suppression of Phase Separation in Lifepo4 Nanoparticles
Suppression of Phase Separation in LiFePO4 Nanoparticles During Battery Discharge Peng Bai,†,§ Daniel A. Cogswell† and Martin Z. Bazant*,†,‡ †Department of Chemical Engineering and ‡Department of Mathematics, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Cambridge, Massachusetts 02139, USA §State Key Laboratory of Automotive Safety and Energy, Department of Automotive Engineering, Tsinghua University, Beijing 100084, P. R. China *Corresponding author: Dr. Martin Z. Bazant. Tel: (617)258-7039; Fax: (617)258-5766; Email: [email protected] August 8, 2011 ABSTRACT: Using a novel electrochemical phase-field model, we question the common belief that LixFePO4 nanoparticles separate into Li-rich and Li-poor phases during battery discharge. For small currents, spinodal decomposition or nucleation leads to moving phase boundaries. Above a critical current density (in the Tafel regime), the spinodal disappears, and particles fill homogeneously, which may explain the superior rate capability and long cycle life of nano-LiFePO4 cathodes. KEYWORDS: Li-ion battery, LiFePO4, phase-field model, Butler-Volmer equation, spinodal decomposition, intercalation waves. 1 Introduction. – LiFePO4-based electrochemical energy storage is one of the most promising developments for electric vehicle power systems and other high-rate applications such as power tools 2,3 and renewable energy storage. Nanoparticles of LiFePO4 have recently been used to demonstrate ultrafast battery discharge4 and high power density carbon pseudocapacitors.5 However, the -
Application of Supercritical Fluids Review Yoshiaki Fukushima
1 Application of Supercritical Fluids Review Yoshiaki Fukushima Abstract Many advantages of supercritical fluids come Supercritical water is expected to be useful in from their interesting or unusual properties which waste treatment. Although they show high liquid solvents and gas carriers do not possess. solubility solutes and molecular catalyses, solvent Such properties and possible applications of molecules under supercritical conditions gently supercritical fluids are reviewed. As these fluids solvate solute molecules and have little influence never condense at above their critical on the activities of the solutes and catalysts. This temperatures, supercritical drying is useful to property would be attributed to the local density prepare dry-gel. The solubility and other fluctuations around each molecule due to high important parameters as a solvent can be adjusted molecular mobility. The fluctuations in the continuously. Supercritical fluids show supercritical fluids would produce heterogeneity advantages as solvents for extraction, coating or that would provide novel chemical reactions with chemical reactions thanks to these properties. molecular catalyses, heterogenous solid catalyses, Supercritical water shows a high organic matter enzymes or solid adsorbents. solubility and a strong hydrolyzing ability. Supercritical fluid, Supercritical water, Solubility, Solvation, Waste treatment, Keywords Coating, Organic reaction applications development reached the initial peak 1. Introduction during the period from the second half of the 1960s There has been rising concern in recent years over to the 1970s followed by the secondary peak about supercritical fluids for organic waste treatment and 15 years later. The initial peak was for the other applications. The discovery of the presence of separation and extraction technique as represented 1) critical point dates back to 1822. -
1504.05850V4.Pdf
Compact Stars in the QCD Phase Diagram IV (CSQCD IV) September 26-30, 2014, Prerow, Germany http://www.ift.uni.wroc.pl/˜csqcdiv Entropic and enthalpic phase transitions in high energy density nuclear matter Igor Iosilevskiy1,2 1 Joint Institute for High Temperatures (Russian Academy of Sciences), Izhorskaya Str. 13/2, 125412 Moscow, Russia 2 Moscow Institute of Physics and Technology (State Research University), Dolgoprudny, 141700, Moscow Region, Russia 1 Abstract Features of Gas-Liquid (GL) and Quark-Hadron (QH) phase transitions (PT) in dense nuclear matter are under discussion in comparison with their terrestrial coun- terparts, e.g. so-called ”plasma” PT in shock-compressed hydrogen, nitrogen etc. Both, GLPT and QHPT, when being represented in widely accepted temperature – baryonic chemical potential plane, are often considered as similar, i.e. amenable to one-to-one mapping by simple scaling. It is argued that this impression is illusive and that GLPT and QHPT belong to different classes: GLPT is typical enthalpic PT (Van-der-Waals-like) while QHPT (”deconfinement-driven”) is typical entropic PT. Subdivision of 1st-order fluid-fluid phase transitions into enthalpic and entropic subclasses was proposed in [arXiv:1403.8053]. Properties of enthalpic and entropic PTs differ significantly. Entropic PT is always internal part of more general and ex- tended thermodynamic anomaly – domains with abnormal (negative) sign for the set of (usually positive) second derivatives of thermodynamic potential, e.g. Gruneizen and thermal expansion and thermal pressure coefficients etc. Negative sign of these derivatives lead to violation of standard behavior and relative order for many iso-lines in P –V plane, e.g. -
Glossary of Terms
GLOSSARY OF TERMS For the purpose of this Handbook, the following definitions and abbreviations shall apply. Although all of the definitions and abbreviations listed below may have not been used in this Handbook, the additional terminology is provided to assist the user of Handbook in understanding technical terminology associated with Drainage Improvement Projects and the associated regulations. Program-specific terms have been defined separately for each program and are contained in pertinent sub-sections of Section 2 of this handbook. ACRONYMS ASTM American Society for Testing Materials CBBEL Christopher B. Burke Engineering, Ltd. COE United States Army Corps of Engineers EPA Environmental Protection Agency IDEM Indiana Department of Environmental Management IDNR Indiana Department of Natural Resources NRCS USDA-Natural Resources Conservation Service SWCD Soil and Water Conservation District USDA United States Department of Agriculture USFWS United States Fish and Wildlife Service DEFINITIONS AASHTO Classification. The official classification of soil materials and soil aggregate mixtures for highway construction used by the American Association of State Highway and Transportation Officials. Abutment. The sloping sides of a valley that supports the ends of a dam. Acre-Foot. The volume of water that will cover 1 acre to a depth of 1 ft. Aggregate. (1) The sand and gravel portion of concrete (65 to 75% by volume), the rest being cement and water. Fine aggregate contains particles ranging from 1/4 in. down to that retained on a 200-mesh screen. Coarse aggregate ranges from 1/4 in. up to l½ in. (2) That which is installed for the purpose of changing drainage characteristics. -
Arxiv:2010.01933V2 [Cond-Mat.Quant-Gas] 18 Feb 2021 Tigated in Refs
Finite temperature spin dynamics of a two-dimensional Bose-Bose atomic mixture Arko Roy,1, ∗ Miki Ota,1, ∗ Alessio Recati,1, 2 and Franco Dalfovo1 1INO-CNR BEC Center and Universit`adi Trento, via Sommarive 14, I-38123 Trento, Italy 2Trento Institute for Fundamental Physics and Applications, INFN, 38123 Povo, Italy We examine the role of thermal fluctuations in uniform two-dimensional binary Bose mixtures of dilute ultracold atomic gases. We use a mean-field Hartree-Fock theory to derive analytical predictions for the miscible-immiscible transition. A nontrivial result of this theory is that a fully miscible phase at T = 0 may become unstable at T 6= 0, as a consequence of a divergent behaviour in the spin susceptibility. We test this prediction by performing numerical simulations with the Stochastic (Projected) Gross-Pitaevskii equation, which includes beyond mean-field effects. We calculate the equilibrium configurations at different temperatures and interaction strengths and we simulate spin oscillations produced by a weak external perturbation. Despite some qualitative agreement, the comparison between the two theories shows that the mean-field approximation is not able to properly describe the behavior of the two-dimensional mixture near the miscible-immiscible transition, as thermal fluctuations smoothen all sharp features both in the phase diagram and in spin dynamics, except for temperature well below the critical temperature for superfluidity. I. INTRODUCTION ing the Popov theory. It is then natural to ask whether such a phase-transition also exists in 2D. The study of phase-separation in two-component clas- It is worth stressing that, in 2D Bose gases, thermal sical fluids is of paramount importance and the role of fluctuations are much more important than in 3D, as they temperature can be rather nontrivial. -
Investigations of Liquid Steel Viscosity and Its Impact As the Initial Parameter on Modeling of the Steel Flow Through the Tundish
materials Article Investigations of Liquid Steel Viscosity and Its Impact as the Initial Parameter on Modeling of the Steel Flow through the Tundish Marta Sl˛ezak´ 1,* and Marek Warzecha 2 1 Department of Ferrous Metallurgy, Faculty of Metals Engineering and Industrial Computer Science, AGH University of Science and Technology, Al. Mickiewicza 30, 30-059 Kraków, Poland 2 Department of Metallurgy and Metal Technology, Faculty of Production Engineering and Materials Technology, Cz˛estochowaUniversity of Technology, Al. Armii Krajowej 19, 42-201 Cz˛estochowa,Poland; [email protected] * Correspondence: [email protected] Received: 14 September 2020; Accepted: 5 November 2020; Published: 7 November 2020 Abstract: The paper presents research carried out to experimentally determine the dynamic viscosity of selected iron solutions. A high temperature rheometer with an air bearing was used for the tests, and ANSYS Fluent commercial software was used for numerical simulations. The experimental results obtained are, on average, lower by half than the values of the dynamic viscosity coefficient of liquid steel adopted during fluid flow modeling. Numerical simulations were carried out, taking into account the viscosity standard adopted for most numerical calculations and the average value of the obtained experimental dynamic viscosity of the analyzed iron solutions. Both qualitative and quantitative analysis showed differences in the flow structure of liquid steel in the tundish, in particular in the predicted values and the velocity profile distribution. However, these differences are not significant. In addition, the work analyzed two different rheological models—including one of our own—to describe the dynamic viscosity of liquid steel, so that in the future, the experimental stage could be replaced by calculating the value of the dynamic viscosity coefficient of liquid steel using one equation. -
Nucleation Initiated Spinodal Decomposition in a Polymerizing System Thein Yk U University of Akron Main Campus, [email protected]
The University of Akron IdeaExchange@UAkron College of Polymer Science and Polymer Engineering 5-1996 Nucleation Initiated Spinodal Decomposition in a Polymerizing System Thein yK u University of Akron Main Campus, [email protected] Jae Hyung Lee University of Akron Main Campus Please take a moment to share how this work helps you through this survey. Your feedback will be important as we plan further development of our repository. Follow this and additional works at: http://ideaexchange.uakron.edu/polymer_ideas Part of the Polymer Science Commons Recommended Citation Kyu, Thein nda Lee, Jae Hyung, "Nucleation Initiated Spinodal Decomposition in a Polymerizing System" (1996). College of Polymer Science and Polymer Engineering. 67. http://ideaexchange.uakron.edu/polymer_ideas/67 This Article is brought to you for free and open access by IdeaExchange@UAkron, the institutional repository of The nivU ersity of Akron in Akron, Ohio, USA. It has been accepted for inclusion in College of Polymer Science and Polymer Engineering by an authorized administrator of IdeaExchange@UAkron. For more information, please contact [email protected], [email protected]. VOLUME 76, NUMBER 20 PHYSICAL REVIEW LETTERS 13MAY 1996 Nucleation Initiated Spinodal Decomposition in a Polymerizing System Thein Kyu and Jae-Hyung Lee Institute of Polymer Engineering, The University of Akron, Akron, Ohio 44325 (Received 29 September 1995) Dynamics of phase separation in a polymerizing system, consisting of carboxyl terminated polybutadiene acrylonitrile/epoxy/methylene dianiline, was investigated by means of time-resolved light scattering. The initial length scale was found to decrease for some early periods of the reaction which has been explained in the context of nucleation initiated spinodal decomposition. -
Plasma Discharge in Water and Its Application for Industrial Cooling Water Treatment
Plasma Discharge in Water and Its Application for Industrial Cooling Water Treatment A Thesis Submitted to the Faculty of Drexel University by Yong Yang In partial fulfillment of the Requirements for the degree of Doctor of Philosophy June 2011 ii © Copyright 2008 Yong Yang. All Rights Reserved. iii Acknowledgements I would like to express my greatest gratitude to both my advisers Prof. Young I. Cho and Prof. Alexander Fridman. Their help, support and guidance were appreciated throughout my graduate studies. Their experience and expertise made my five year at Drexel successful and enjoyable. I would like to convey my deep appreciation to the most dedicated Dr. Alexander Gutsol and Dr. Andrey Starikovskiy, with whom I had pleasure to work with on all these projects. I feel thankful for allowing me to walk into their office any time, even during their busiest hours, and I’m always amazed at the width and depth of their knowledge in plasma physics. Also I would like to thank Profs. Ying Sun, Gary Friedman, and Alexander Rabinovich for their valuable advice on this thesis as committee members. I am thankful for the financial support that I received during my graduate study, especially from the DOE grants DE-FC26-06NT42724 and DE-NT0005308, the Drexel Dean’s Fellowship, George Hill Fellowship, and the support from the Department of Mechanical Engineering and Mechanics. I would like to thank the friendship and help from the friends and colleagues at Drexel Plasma Institute over the years. Special thanks to Hyoungsup Kim and Jin Mu Jung. Without their help I would not be able to finish the fouling experiments alone. -
Spinodal Lines and Equations of State: a Review
10 l Nuclear Engineering and Design 95 (1986) 297-314 297 North-Holland, Amsterdam SPINODAL LINES AND EQUATIONS OF STATE: A REVIEW John H. LIENHARD, N, SHAMSUNDAR and PaulO, BINEY * Heat Transfer/ Phase-Change Laboratory, Mechanical Engineering Department, University of Houston, Houston, TX 77004, USA The importance of knowing superheated liquid properties, and of locating the liquid spinodal line, is discussed, The measurement and prediction of the spinodal line, and the limits of isentropic pressure undershoot, are reviewed, Means are presented for formulating equations of state and fundamental equations to predict superheated liquid properties and spinodal limits, It is shown how the temperature dependence of surface tension can be used to verify p - v - T equations of state, or how this dependence can be predicted if the equation of state is known. 1. Scope methods for making simplified predictions of property information, which can be applied to the full range of Today's technology, with its emphasis on miniaturiz fluids - water, mercury, nitrogen, etc. [3-5]; and predic ing and intensifying thennal processes, steadily de tions of the depressurizations that might occur in ther mands higher heat fluxes and poses greater dangers of mohydraulic accidents. (See e.g. refs. [6,7].) sending liquids beyond their boiling points into the metastable, or superheated, state. This state poses the threat of serious thermohydraulic explosions. Yet we 2. The spinodal limit of liquid superheat know little about its thermal properties, and cannot predict process behavior after a liquid becomes super heated. Some of the practical situations that require a 2.1. The role of the equation of state in defining the spinodal line knowledge the limits of liquid superheat, and the physi cal properties of superheated liquids, include: - Thennohydraulic explosions as might occur in nuclear Fig. -
Notes on Phase Seperation Chem 130A Fall 2002 Prof
Notes on Phase Seperation Chem 130A Fall 2002 Prof. Groves Consider the process: Pure 1 + Pure 2 Æ Mixture of 1 and 2 We have previously derived the entropy of mixing for this process from statistical principles and found it to be: ∆ =− − Smix kN11ln X kN 2 ln X 2 where N1 and N2 are the number of molecules of type 1 and 2, respectively. We use k, the Boltzmann constant, since N1 and N2 are number of molecules. We could alternatively use R, the gas constant, if we chose to represent the number of molecules in terms of moles. X1 and X2 represent the mole fraction (e.g. X1 = N1 / (N1+N2)) of 1 and 2, respectively. If there are interactions between the two ∆ components, there will be a non-zero Hmix that we must consider. We can derive an expression ∆H = 2γ ∆ ∆ for Hmix using H of swapping one molecule of type 1, in pure type 1, with one molecule of type 2, in pure type 2 (see adjacent figure). We define γ as half of this ∆H of interchange. It is a differential interaction energy that tells us the energy difference between 1:1 and 2:2 interactions and 1:2 interactions. By defining 2γ = ∆H, γ represents the energy change associated with one molecule (note that two were involved in the swap). ∆ γ Now, to calculate Hmix from , we first consider 1 molecule of type 1 in the mixed system. For the moment we need not be concerned with whether or not they actually will mix, we just want ∆ to calculate Hmix as if they mix thoroughly.