An Equation of State for the Thermodynamic Properties of Cyclohexane Yong Zhou, Jun Liu, Steven G
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Physical Model for Vaporization
Physical model for vaporization Jozsef Garai Department of Mechanical and Materials Engineering, Florida International University, University Park, VH 183, Miami, FL 33199 Abstract Based on two assumptions, the surface layer is flexible, and the internal energy of the latent heat of vaporization is completely utilized by the atoms for overcoming on the surface resistance of the liquid, the enthalpy of vaporization was calculated for 45 elements. The theoretical values were tested against experiments with positive result. 1. Introduction The enthalpy of vaporization is an extremely important physical process with many applications to physics, chemistry, and biology. Thermodynamic defines the enthalpy of vaporization ()∆ v H as the energy that has to be supplied to the system in order to complete the liquid-vapor phase transformation. The energy is absorbed at constant pressure and temperature. The absorbed energy not only increases the internal energy of the system (U) but also used for the external work of the expansion (w). The enthalpy of vaporization is then ∆ v H = ∆ v U + ∆ v w (1) The work of the expansion at vaporization is ∆ vw = P ()VV − VL (2) where p is the pressure, VV is the volume of the vapor, and VL is the volume of the liquid. Several empirical and semi-empirical relationships are known for calculating the enthalpy of vaporization [1-16]. Even though there is no consensus on the exact physics, there is a general agreement that the surface energy must be an important part of the enthalpy of vaporization. The vaporization diminishes the surface energy of the liquid; thus this energy must be supplied to the system. -
Physics, Chapter 17: the Phases of Matter
University of Nebraska - Lincoln DigitalCommons@University of Nebraska - Lincoln Robert Katz Publications Research Papers in Physics and Astronomy 1-1958 Physics, Chapter 17: The Phases of Matter Henry Semat City College of New York Robert Katz University of Nebraska-Lincoln, [email protected] Follow this and additional works at: https://digitalcommons.unl.edu/physicskatz Part of the Physics Commons Semat, Henry and Katz, Robert, "Physics, Chapter 17: The Phases of Matter" (1958). Robert Katz Publications. 165. https://digitalcommons.unl.edu/physicskatz/165 This Article is brought to you for free and open access by the Research Papers in Physics and Astronomy at DigitalCommons@University of Nebraska - Lincoln. It has been accepted for inclusion in Robert Katz Publications by an authorized administrator of DigitalCommons@University of Nebraska - Lincoln. 17 The Phases of Matter 17-1 Phases of a Substance A substance which has a definite chemical composition can exist in one or more phases, such as the vapor phase, the liquid phase, or the solid phase. When two or more such phases are in equilibrium at any given temperature and pressure, there are always surfaces of separation between the two phases. In the solid phase a pure substance generally exhibits a well-defined crystal structure in which the atoms or molecules of the substance are arranged in a repetitive lattice. Many substances are known to exist in several different solid phases at different conditions of temperature and pressure. These solid phases differ in their crystal structure. Thus ice is known to have six different solid phases, while sulphur has four different solid phases. -
Chapter 3 Equations of State
Chapter 3 Equations of State The simplest way to derive the Helmholtz function of a fluid is to directly integrate the equation of state with respect to volume (Sadus, 1992a, 1994). An equation of state can be applied to either vapour-liquid or supercritical phenomena without any conceptual difficulties. Therefore, in addition to liquid-liquid and vapour -liquid properties, it is also possible to determine transitions between these phenomena from the same inputs. All of the physical properties of the fluid except ideal gas are also simultaneously calculated. Many equations of state have been proposed in the literature with either an empirical, semi- empirical or theoretical basis. Comprehensive reviews can be found in the works of Martin (1979), Gubbins (1983), Anderko (1990), Sandler (1994), Economou and Donohue (1996), Wei and Sadus (2000) and Sengers et al. (2000). The van der Waals equation of state (1873) was the first equation to predict vapour-liquid coexistence. Later, the Redlich-Kwong equation of state (Redlich and Kwong, 1949) improved the accuracy of the van der Waals equation by proposing a temperature dependence for the attractive term. Soave (1972) and Peng and Robinson (1976) proposed additional modifications of the Redlich-Kwong equation to more accurately predict the vapour pressure, liquid density, and equilibria ratios. Guggenheim (1965) and Carnahan and Starling (1969) modified the repulsive term of van der Waals equation of state and obtained more accurate expressions for hard sphere systems. Christoforakos and Franck (1986) modified both the attractive and repulsive terms of van der Waals equation of state. Boublik (1981) extended the Carnahan-Starling hard sphere term to obtain an accurate equation for hard convex geometries. -
Liquid-Vapor Equilibrium in a Binary System
Liquid-Vapor Equilibria in Binary Systems1 Purpose The purpose of this experiment is to study a binary liquid-vapor equilibrium of chloroform and acetone. Measurements of liquid and vapor compositions will be made by refractometry. The data will be treated according to equilibrium thermodynamic considerations, which are developed in the theory section. Theory Consider a liquid-gas equilibrium involving more than one species. By definition, an ideal solution is one in which the vapor pressure of a particular component is proportional to the mole fraction of that component in the liquid phase over the entire range of mole fractions. Note that no distinction is made between solute and solvent. The proportionality constant is the vapor pressure of the pure material. Empirically it has been found that in very dilute solutions the vapor pressure of solvent (major component) is proportional to the mole fraction X of the solvent. The proportionality constant is the vapor pressure, po, of the pure solvent. This rule is called Raoult's law: o (1) psolvent = p solvent Xsolvent for Xsolvent = 1 For a truly ideal solution, this law should apply over the entire range of compositions. However, as Xsolvent decreases, a point will generally be reached where the vapor pressure no longer follows the ideal relationship. Similarly, if we consider the solute in an ideal solution, then Eq.(1) should be valid. Experimentally, it is generally found that for dilute real solutions the following relationship is obeyed: psolute=K Xsolute for Xsolute<< 1 (2) where K is a constant but not equal to the vapor pressure of pure solute. -
Corollary from the Exact Expression for Enthalpy of Vaporization
Hindawi Publishing Corporation Journal of Thermodynamics Volume 2011, Article ID 945047, 7 pages doi:10.1155/2011/945047 Research Article Corollary from the Exact Expression for Enthalpy of Vaporization A. A. Sobko Department of Physics and Chemistry of New Materials, A. M. Prokhorov Academy of Engineering Sciences, 19 Presnensky Val, Moscow 123557, Russia Correspondence should be addressed to A. A. Sobko, [email protected] Received 14 November 2010; Revised 9 March 2011; Accepted 16 March 2011 Academic Editor: K. A. Antonopoulos Copyright © 2011 A. A. Sobko. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. A problem on determining effective volumes for atoms and molecules becomes actual due to rapidly developing nanotechnologies. In the present study an exact expression for enthalpy of vaporization is obtained, from which an exact expression is derived for effective volumes of atoms and molecules, and under certain assumptions on the form of an atom (molecule) it is possible to find their linear dimensions. The accuracy is only determined by the accuracy of measurements of thermodynamic parameters at the critical point. 1. Introduction 1938 [2] with the edition from 1976 [3], we may find them actually similar. we may come to the same conclusion if In the present study, the relationship is obtained that we compare [2] with recent monograph by Prigogine and combines the enthalpy of vaporization with other thermody- Kondepudi “Modern Thermodynamics” [4]. The chapters namic evaporation parameters from the general expression devoted to first-order phase transitions in both monographs for the heat of first-order phase transformations. -
Liquid Equilibrium Measurements in Binary Polar Systems
DIPLOMA THESIS VAPOR – LIQUID EQUILIBRIUM MEASUREMENTS IN BINARY POLAR SYSTEMS Supervisors: Univ. Prof. Dipl.-Ing. Dr. Anton Friedl Associate Prof. Epaminondas Voutsas Antonia Ilia Vienna 2016 Acknowledgements First of all I wish to thank Doctor Walter Wukovits for his guidance through the whole project, great assistance and valuable suggestions for my work. I have completed this thesis with his patience, persistence and encouragement. Secondly, I would like to thank Professor Anton Friedl for giving me the opportunity to work in TU Wien and collaborate with him and his group for this project. I am thankful for his trust from the beginning until the end and his support during all this period. Also, I wish to thank for his readiness to help and support Professor Epaminondas Voutsas, who gave me the opportunity to carry out this thesis in TU Wien, and his valuable suggestions and recommendations all along the experimental work and calculations. Additionally, I would like to thank everybody at the office and laboratory at TU Wien for their comprehension and selfless help for everything I needed. Furthermore, I wish to thank Mersiha Gozid and all the students of Chemical Engineering Summer School for their contribution of data, notices, questions and solutions during my experimental work. And finally, I would like to thank my family and friends for their endless support and for the inspiration and encouragement to pursue my goals and dreams. Abstract An experimental study was conducted in order to investigate the vapor – liquid equilibrium of binary mixtures of Ethanol – Butan-2-ol, Methanol – Ethanol, Methanol – Butan-2-ol, Ethanol – Water, Methanol – Water, Acetone – Ethanol and Acetone – Butan-2-ol at ambient pressure using the dynamic apparatus Labodest VLE 602. -
Problem Set #10 Assigned November 8, 2013 – Due Friday, November 15, 2013 Please Show All Work for Credit
Problem Set #10 Assigned November 8, 2013 – Due Friday, November 15, 2013 Please show all work for credit To Hand in 1. 1 2. –1 A least squares fit of ln P versus 1/T gives the result Hvaporization = 25.28 kJ mol . 3. Assuming constant pressure and temperature, and that the surface area of the protein is reduced by 25% due to the hydrophobic interaction: 2 G 0.25 N A 4 r Convert to per mole, ↓determine size per molecule 4 r 3 V M N 0.73mL/ g 60000g / mol (6.02 1023) 3 2 2 A r 2.52 109 m 2 23 9 2 G 0.25 N A 4 r 0.0720N / m 0.25 6.02 10 / mol (4 ) (2.52 10 m) 865kJ / mol We think this is a reasonable approach, but the value seems high 2 4. The vapor pressure of an unknown solid is approximately given by ln(P/Torr) = 22.413 – 2035(K/T), and the vapor pressure of the liquid phase of the same substance is approximately given by ln(P/Torr) = 18.352 – 1736(K/T). a. Calculate Hvaporization and Hsublimation. b. Calculate Hfusion. c. Calculate the triple point temperature and pressure. a) Calculate Hvaporization and Hsublimation. From Equation (8.16) dPln H sublimation dT RT 2 dln P d ln P dT d ln P H T 2 sublimation 11 dT dT R dd TT For this specific case H sublimation 2035 H 16.92 103 J mol –1 R sublimation Following the same proedure as above, H vaporization 1736 H 14.43 103 J mol –1 R vaporization b. -
Phase Diagrams a Phase Diagram Is Used to Show the Relationship Between Temperature, Pressure and State of Matter
Phase Diagrams A phase diagram is used to show the relationship between temperature, pressure and state of matter. Before moving ahead, let us review some vocabulary and particle diagrams. States of Matter Solid: rigid, has definite volume and definite shape Liquid: flows, has definite volume, but takes the shape of the container Gas: flows, no definite volume or shape, shape and volume are determined by container Plasma: atoms are separated into nuclei (neutrons and protons) and electrons, no definite volume or shape Changes of States of Matter Freezing start as a liquid, end as a solid, slowing particle motion, forming more intermolecular bonds Melting start as a solid, end as a liquid, increasing particle motion, break some intermolecular bonds Condensation start as a gas, end as a liquid, decreasing particle motion, form intermolecular bonds Evaporation/Boiling/Vaporization start as a liquid, end as a gas, increasing particle motion, break intermolecular bonds Sublimation Starts as a solid, ends as a gas, increases particle speed, breaks intermolecular bonds Deposition Starts as a gas, ends as a solid, decreases particle speed, forms intermolecular bonds http://phet.colorado.edu/en/simulation/states- of-matter The flat sections on the graph are the points where a phase change is occurring. Both states of matter are present at the same time. In the flat sections, heat is being removed by the formation of intermolecular bonds. The flat points are phase changes. The heat added to the system are being used to break intermolecular bonds. PHASE DIAGRAMS Phase diagrams are used to show when a specific substance will change its state of matter (alignment of particles and distance between particles). -
Vapor Pressures and Vaporization Enthalpies of the N-Alkanes from 2 C21 to C30 at T ) 298.15 K by Correlation Gas Chromatography
BATCH: je1a04 USER: jeh69 DIV: @xyv04/data1/CLS_pj/GRP_je/JOB_i01/DIV_je0301747 DATE: October 17, 2003 1 Vapor Pressures and Vaporization Enthalpies of the n-Alkanes from 2 C21 to C30 at T ) 298.15 K by Correlation Gas Chromatography 3 James S. Chickos* and William Hanshaw 4 Department of Chemistry and Biochemistry, University of MissourisSt. Louis, St. Louis, Missouri 63121 5 6 The temperature dependence of gas chromatographic retention times for n-heptadecane to n-triacontane 7 is reported. These data are used to evaluate the vaporization enthalpies of these compounds at T ) 298.15 8 K, and a protocol is described that provides vapor pressures of these n-alkanes from T ) 298.15 to 575 9 K. The vapor pressure and vaporization enthalpy results obtained are compared with existing literature 10 data where possible and found to be internally consistent. Sublimation enthalpies for n-C17 to n-C30 are 11 calculated by combining vaporization enthalpies with fusion enthalpies and are compared when possible 12 to direct measurements. 13 14 Introduction 15 The n-alkanes serve as excellent standards for the 16 measurement of vaporization enthalpies of hydrocarbons.1,2 17 Recently, the vaporization enthalpies of the n-alkanes 18 reported in the literature were examined and experimental 19 values were selected on the basis of how well their 20 vaporization enthalpies correlated with their enthalpies of 21 transfer from solution to the gas phase as measured by gas 22 chromatography.3 A plot of the vaporization enthalpies of 23 the n-alkanes as a function of the number of carbon atoms 24 is given in Figure 1. -
Measured and Predicted Vapor Liquid Equilibrium
NREL/CP-5400-71336. Posted with permission. Presented at WCX18: SAE World Congress Experience, 10-12 April 2018, Detroit, Michigan. 2018-01-0361 Published 03 Apr 2018 Measured and Predicted Vapor Liquid Equilibrium of Ethanol-Gasoline Fuels with Insight on the Influence of Azeotrope Interactions on Aromatic Species Enrichment and Particulate Matter Formation in Spark Ignition Engines Stephen Burke Colorado State University Robert Rhoads University of Colorado Matthew Ratcliff and Robert McCormick National Renewable Energy Laboratory Bret Windom Colorado State University Citation: Burke, S., Rhoads, R., Ratcliff, M., McCormick, R. et al., “Measured and Predicted Vapor Liquid Equilibrium of Ethanol-Gasoline Fuels with Insight on the Influence of Azeotrope Interactions on Aromatic Species Enrichment and Particulate Matter Formation in Spark Ignition Engines,” SAE Technical Paper 2018-01-0361, 2018, doi:10.4271/2018-01-0361. Abstract the azeotrope interactions on the vapor/liquid composition relationship has been observed between increasing evolution of the fuel, distillations were performed using the ethanol content in gasoline and increased particulate Advanced Distillation Curve apparatus on carefully selected Amatter (PM) emissions from direct injection spark samples consisting of gasoline blended with ethanol and heavy ignition (DISI) vehicles. The fundamental cause of this obser- aromatic and oxygenated compounds with varying vapor pres- vation is not well understood. One potential explanation is sures, including cumene, p-cymene, 4-tertbutyl toluene, that increased evaporative cooling as a result of ethanol’s high anisole, and 4-methyl anisole. Samples collected during the HOV may slow evaporation and prevent sufficient reactant distillation indicate an enrichment of the heavy aromatic or mixing resulting in the combustion of localized fuel rich oxygenated additive with an increase in initial ethanol concen- regions within the cylinder. -
Understanding Vapor Diffusion and Condensation
uilding enclosure assemblies temperature is the temperature at which the moisture content, age, temperature, and serve a variety of functions RH of the air would be 100%. This is also other factors. Vapor resistance is commonly to deliver long-lasting sepa- the temperature at which condensation will expressed using the inverse term “vapor ration of the interior building begin to occur. permeance,” which is the relative ease of environment from the exteri- The direction of vapor diffusion flow vapor diffusion through a material. or, one of which is the control through an assembly is always from the Vapor-retarding materials are often Bof vapor diffusion. Resistance to vapor diffu- high vapor pressure side to the low vapor grouped into classes (Classes I, II, III) sion is part of the environmental separation; pressure side, which is often also from the depending on their vapor permeance values. however, vapor diffusion control is often warm side to the cold side, because warm Class I (<0.1 US perm) and Class II (0.1 to primarily provided to avoid potentially dam- air can hold more water than cold air (see 1.0 US perm) vapor retarder materials are aging moisture accumulation within build- Figure 2). Importantly, this means it is not considered impermeable to near-imperme- ing enclosure assemblies. While resistance always from the higher RH side to the lower able, respectively, and are known within to vapor diffusion in wall assemblies has RH side. the industry as “vapor barriers.” Some long been understood, ever-increasing ener- The direction of the vapor drive has materials that fall into this category include gy code requirements have led to increased important ramifications with respect to the polyethylene sheet, sheet metal, aluminum insulation levels, which in turn have altered placement of materials within an assembly, foil, some foam plastic insulations (depend- the way assemblies perform with respect to and what works in one climate may not work ing on thickness), and self-adhered (peel- vapor diffusion and condensation control. -
Sub-Slab Vapor Sampling Procedures
Sub-Slab Vapor Sampling Procedures RR-986 July 2014 Table of Contents I. Introduction .......................................................................................................................... 2 II. Sub-Slab Sample Ports .......................................................................................................... 2 A. Distribution of sub-slab probes ...................................................................................... 3 B. Permanent vs. temporary sub-slab probes .................................................................... 4 C. Tubing used in the sample train ..................................................................................... 4 D. Abandonment of sub-slab probes .................................................................................. 4 E. Sub-slab vapor samples collected from a sump pit ....................................................... 4 III. Leak Testing and Collecting a Sub-slab Sample .................................................................... 5 A. Shut-in test ..................................................................................................................... 6 B. Helium shroud ................................................................................................................ 7 C. Other leak detection methods for probe seals .............................................................. 7 D. Sample collection after leak testing ............................................................................... 8