Lecture 8: Surface Tension, Internal Pressure and Energy of a Spherical Particle Or Droplet
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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. -
Atwood's Machine? (5 Points)
rev 09/2019 Atwood’s Machine Equipment Qty Equipment Part Number 1 Mass and Hanger Set ME‐8979 1 Photogate with Pully ME‐6838A 1 Universal Table Clamp ME‐9376B 1 Large Rod ME‐8736 1 Small Rod ME‐8977 1 Double rod Clamp ME‐9873 1 String Background Newton’s 2nd Law (NSL) states that the acceleration a mass experiences is proportional to the net force applied to it, and inversely proportional to its inertial mass ( ). An Atwood’s Machine is a simple device consisting of a pulley, with two masses connected by a string that runs over the pulley. For an ‘ideal Atwood’s Machine’ we assume the pulley is massless, and frictionless, that the string is unstretchable, therefore a constant length, and also massless. Consider the following diagram of an ideal Atwood’s machine. One of the standard ways to apply NSL is to draw Free Body Diagrams for the masses in the system, then write Force Summation Equations for each Free Body Diagram. We will use the standard practice of labeling masses from smallest to largest, therefore m2 > m1. For an Atwood’s Machine there are only forces acting on the masses in the vertical direction so we will only need to write Force Summation Equations for the y‐direction. We obtain the following Free Body Diagrams for the two masses. Each of the masses have two forces acting on it. Each has its own weight (m1g, or m2g) pointing downwards, and each has the tension (T) in the string pointing upwards. By the assumption of an ideal string the tension is the same throughout the string. -
Chapter 3. Second and Third Law of Thermodynamics
Chapter 3. Second and third law of thermodynamics Important Concepts Review Entropy; Gibbs Free Energy • Entropy (S) – definitions Law of Corresponding States (ch 1 notes) • Entropy changes in reversible and Reduced pressure, temperatures, volumes irreversible processes • Entropy of mixing of ideal gases • 2nd law of thermodynamics • 3rd law of thermodynamics Math • Free energy Numerical integration by computer • Maxwell relations (Trapezoidal integration • Dependence of free energy on P, V, T https://en.wikipedia.org/wiki/Trapezoidal_rule) • Thermodynamic functions of mixtures Properties of partial differential equations • Partial molar quantities and chemical Rules for inequalities potential Major Concept Review • Adiabats vs. isotherms p1V1 p2V2 • Sign convention for work and heat w done on c=C /R vm system, q supplied to system : + p1V1 p2V2 =Cp/CV w done by system, q removed from system : c c V1T1 V2T2 - • Joule-Thomson expansion (DH=0); • State variables depend on final & initial state; not Joule-Thomson coefficient, inversion path. temperature • Reversible change occurs in series of equilibrium V states T TT V P p • Adiabatic q = 0; Isothermal DT = 0 H CP • Equations of state for enthalpy, H and internal • Formation reaction; enthalpies of energy, U reaction, Hess’s Law; other changes D rxn H iD f Hi i T D rxn H Drxn Href DrxnCpdT Tref • Calorimetry Spontaneous and Nonspontaneous Changes First Law: when one form of energy is converted to another, the total energy in universe is conserved. • Does not give any other restriction on a process • But many processes have a natural direction Examples • gas expands into a vacuum; not the reverse • can burn paper; can't unburn paper • heat never flows spontaneously from cold to hot These changes are called nonspontaneous changes. -
THE SOLUBILITY of GASES in LIQUIDS Introductory Information C
THE SOLUBILITY OF GASES IN LIQUIDS Introductory Information C. L. Young, R. Battino, and H. L. Clever INTRODUCTION The Solubility Data Project aims to make a comprehensive search of the literature for data on the solubility of gases, liquids and solids in liquids. Data of suitable accuracy are compiled into data sheets set out in a uniform format. The data for each system are evaluated and where data of sufficient accuracy are available values are recommended and in some cases a smoothing equation is given to represent the variation of solubility with pressure and/or temperature. A text giving an evaluation and recommended values and the compiled data sheets are published on consecutive pages. The following paper by E. Wilhelm gives a rigorous thermodynamic treatment on the solubility of gases in liquids. DEFINITION OF GAS SOLUBILITY The distinction between vapor-liquid equilibria and the solubility of gases in liquids is arbitrary. It is generally accepted that the equilibrium set up at 300K between a typical gas such as argon and a liquid such as water is gas-liquid solubility whereas the equilibrium set up between hexane and cyclohexane at 350K is an example of vapor-liquid equilibrium. However, the distinction between gas-liquid solubility and vapor-liquid equilibrium is often not so clear. The equilibria set up between methane and propane above the critical temperature of methane and below the criti cal temperature of propane may be classed as vapor-liquid equilibrium or as gas-liquid solubility depending on the particular range of pressure considered and the particular worker concerned. -
Pressure Diffusion Waves in Porous Media
Lawrence Berkeley National Laboratory Lawrence Berkeley National Laboratory Title Pressure diffusion waves in porous media Permalink https://escholarship.org/uc/item/5bh9f6c4 Authors Silin, Dmitry Korneev, Valeri Goloshubin, Gennady Publication Date 2003-04-08 eScholarship.org Powered by the California Digital Library University of California Pressure diffusion waves in porous media Dmitry Silin* and Valeri Korneev, Lawrence Berkeley National Laboratory, Gennady Goloshubin, University of Houston Summary elastic porous medium. Such a model results in a parabolic pressure diffusion equation. Its validity has been Pressure diffusion wave in porous rocks are under confirmed and “canonized”, for instance, in transient consideration. The pressure diffusion mechanism can pressure well test analysis, where it is used as the main tool provide an explanation of the high attenuation of low- since 1930th, see e.g. Earlougher (1977) and Barenblatt et. frequency signals in fluid-saturated rocks. Both single and al., (1990). The basic assumptions of this model make it dual porosity models are considered. In either case, the applicable specifically in the low-frequency range of attenuation coefficient is a function of the frequency. pressure fluctuations. Introduction Theories describing wave propagation in fluid-bearing porous media are usually derived from Biot’s theory of poroelasticity (Biot 1956ab, 1962). However, the observed high attenuation of low-frequency waves (Goloshubin and Korneev, 2000) is not well predicted by this theory. One of possible reasons for difficulties in detecting Biot waves in real rocks is in the limitations imposed by the assumptions underlying Biot’s equations. Biot (1956ab, 1962) derived his main equations characterizing the mechanical motion of elastic porous fluid-saturated rock from the Hamiltonian Principle of Least Action. -
Surface Structure, Chemisorption and Reactions
Surface Structure, Chemisorption and Reactions Eckhard Pehlke, Institut für Theoretische Physik und Astrophysik, Christian-Albrechts-Universität zu Kiel, 24098 Kiel, Germany. Topics: (i) interplay between the geometric and electronic structure of solid surfaces, (ii) physical properties of surfaces: surface energy, surface stress and their relevance for surface morphology (iii) adsorption and desorption energy barriers, chemical reactivity of surfaces, heterogeneous catalysis (iv) chemisorption dynamics and energy dissipation: electronically non-adiabatic processes Technological Importance of Surfaces Solid surfaces are intriguing objects for basic research, and they are also of high technological utility: substrates for homo- or hetero-epitaxial growth of semiconductor thin films used in device technology surfaces can act as heterogeneous catalysts, used to induce and steer the desired chemical reactions Sect. I: The Geometric and the Electronic Structure of Crystal Surfaces Surface Crystallography 2D 3D number of space groups: 17 230 number of point groups: 10 32 number of Bravais lattices: 5 14 2D- symbol lattice 2D Bravais space point crystal system parameters lattice group groups m mp 1 oblique (mono- γ b 2 a, b, γ 2 clin) a o op b (ortho- a, b a m rectangular rhom- o 7 γ = 90 2mm bic) oc b a t (tetra- a = b 4 o tp a 3 square gonal) γ = 90 a 4mm a h hp 3 o a hexagonal (hexa- a = b 120 6 o gonal) γ = 120 5 3m 6mm Bulk Terminated fcc Crystal Surfaces z z fcc a (010) x y c a=c/ √ 2 x square lattice (tp) z z fcc (110) a c _ [110] y x rectangular lattice (op) z _ (111) fcc [011] _ [110] a y hexagonal lattice (hp) x Surface Atomic Geometry Examples: a reduced inter-layer H/Si(111) separation normal relaxation 2a Si(111) (7x7) (2x1) reconstruction K. -
What Is High Blood Pressure?
ANSWERS Lifestyle + Risk Reduction by heart High Blood Pressure BLOOD PRESSURE SYSTOLIC mm Hg DIASTOLIC mm Hg What is CATEGORY (upper number) (lower number) High Blood NORMAL LESS THAN 120 and LESS THAN 80 ELEVATED 120-129 and LESS THAN 80 Pressure? HIGH BLOOD PRESSURE 130-139 or 80-89 (HYPERTENSION) Blood pressure is the force of blood STAGE 1 pushing against blood vessel walls. It’s measured in millimeters of HIGH BLOOD PRESSURE 140 OR HIGHER or 90 OR HIGHER mercury (mm Hg). (HYPERTENSION) STAGE 2 High blood pressure (HBP) means HYPERTENSIVE the pressure in your arteries is higher CRISIS HIGHER THAN 180 and/ HIGHER THAN 120 than it should be. Another name for (consult your doctor or immediately) high blood pressure is hypertension. Blood pressure is written as two numbers, such as 112/78 mm Hg. The top, or larger, number (called Am I at higher risk of developing HBP? systolic pressure) is the pressure when the heart There are risk factors that increase your chances of developing HBP. Some you can control, and some you can’t. beats. The bottom, or smaller, number (called diastolic pressure) is the pressure when the heart Those that can be controlled are: rests between beats. • Cigarette smoking and exposure to secondhand smoke • Diabetes Normal blood pressure is below 120/80 mm Hg. • Being obese or overweight If you’re an adult and your systolic pressure is 120 to • High cholesterol 129, and your diastolic pressure is less than 80, you have elevated blood pressure. High blood pressure • Unhealthy diet (high in sodium, low in potassium, and drinking too much alcohol) is a systolic pressure of 130 or higher,or a diastolic pressure of 80 or higher, that stays high over time. -
THE SOLUBILITY of GASES in LIQUIDS INTRODUCTION the Solubility Data Project Aims to Make a Comprehensive Search of the Lit- Erat
THE SOLUBILITY OF GASES IN LIQUIDS R. Battino, H. L. Clever and C. L. Young INTRODUCTION The Solubility Data Project aims to make a comprehensive search of the lit erature for data on the solubility of gases, liquids and solids in liquids. Data of suitable accuracy are compiled into data sheets set out in a uni form format. The data for each system are evaluated and where data of suf ficient accuracy are available values recommended and in some cases a smoothing equation suggested to represent the variation of solubility with pressure and/or temperature. A text giving an evaluation and recommended values and the compiled data sheets are pUblished on consecutive pages. DEFINITION OF GAS SOLUBILITY The distinction between vapor-liquid equilibria and the solUbility of gases in liquids is arbitrary. It is generally accepted that the equilibrium set up at 300K between a typical gas such as argon and a liquid such as water is gas liquid solubility whereas the equilibrium set up between hexane and cyclohexane at 350K is an example of vapor-liquid equilibrium. However, the distinction between gas-liquid solUbility and vapor-liquid equilibrium is often not so clear. The equilibria set up between methane and propane above the critical temperature of methane and below the critical temperature of propane may be classed as vapor-liquid equilibrium or as gas-liquid solu bility depending on the particular range of pressure considered and the par ticular worker concerned. The difficulty partly stems from our inability to rigorously distinguish between a gas, a vapor, and a liquid, which has been discussed in numerous textbooks. -
Statistical Mechanics I: Exam Review 1 Solution
8.333: Statistical Mechanics I Fall 2007 Test 1 Review Problems The first in-class test will take place on Wednesday 9/26/07 from 2:30 to 4:00 pm. There will be a recitation with test review on Friday 9/21/07. The test is ‘closed book,’ but if you wish you may bring a one-sided sheet of formulas. The test will be composed entirely from a subset of the following problems. Thus if you are familiar and comfortable with these problems, there will be no surprises! ******** You may find the following information helpful: Physical Constants 31 27 Electron mass me 9.1 10− kg Proton mass mp 1.7 10− kg ≈ × 19 ≈ × 34 1 Electron Charge e 1.6 10− C Planck’s const./2π ¯h 1.1 10− Js− ≈ × 8 1 ≈ × 8 2 4 Speed of light c 3.0 10 ms− Stefan’s const. σ 5.7 10− W m− K− ≈ × 23 1 ≈ × 23 1 Boltzmann’s const. k 1.4 10− JK− Avogadro’s number N 6.0 10 mol− B ≈ × 0 ≈ × Conversion Factors 5 2 10 4 1atm 1.0 10 Nm− 1A˚ 10− m 1eV 1.1 10 K ≡ × ≡ ≡ × Thermodynamics dE = T dS+dW¯ For a gas: dW¯ = P dV For a wire: dW¯ = Jdx − Mathematical Formulas √π ∞ n αx n! 1 0 dx x e− = αn+1 2 ! = 2 R 2 2 2 ∞ x √ 2 σ k dx exp ikx 2σ2 = 2πσ exp 2 limN ln N! = N ln N N −∞ − − − →∞ − h i h i R n n ikx ( ik) n ikx ( ik) n e− = ∞ − x ln e− = ∞ − x n=0 n! � � n=1 n! � �c P 2 4 P 3 5 cosh(x) = 1 + x + x + sinh(x) = x + x + x + 2! 4! · · · 3! 5! · · · 2πd/2 Surface area of a unit sphere in d dimensions Sd = (d/2 1)! − 1 1. -
Interfaces in Aquatic Ecosystems: Implications for Transport and Impact of I Anthropogenic Compounds Luhbds-«6KE---C)I‘> "Rol°
Interfaces in aquatic ecosystems: Implications for transport and impact of I anthropogenic compounds luhbDS-«6KE---c)I‘> "rol° STER DISTfiStihON OF THIS DOCUMENT iS UNUMITED % In memory of Fetter, victim of human negligence and To my family andfriends Organization Document name LUND UNIVERSITY DOCTORAL DISSERTATION Department of Ecology Date of issue November 19, 1996 Chemical Ecology and Ecotoxicology Ecology Building CODEN: SE- LUNBDS/NBKE-96/1010+136 S-223 62 Lund, Sweden Authors) Sponsoring organization Swedish Environ JOHANNES KNULST mental Research Institute (IVL) Title and subtitle Interfaces in aquatic ecosystems : Implications for transport and impact of anthropogenic compounds Abstract Mechanisms that govern transport, accumulation and toxicity of persistent pollutants at interfaces in aquatic ecosystems were the foci of this thesis . Specific attention was paid to humic substances, their occurrence, composition, and role in exchange processes across interfaces. It was concluded that: The composition of humic substances in aquatic surface microlavers is different from that of the subsurface water and terrestrial humic mat ter. Levels of dissolved organic carbon (DOC)in the aquatic surface micro layer reflect the DOC levels in the subsurface water. While the levels and enrichment of DOC in the microlaver generally show small variations, the levels and enrichment of particulate organic car bon (POC) vary to a great extent. Similarities exist between aquatic surface films, artificial semi-per meable and biological membranes regarding their structure and function ing. Acidification and liming of freshwater ecosystems affect DOC:POC ratio and humic composition of the surface film, thus influencing the parti tioning of pollutants across aquatic interfaces. 21 Properties of lake catchment areas extensively govern DOC:POC ratio both 41 in the surface film and subsurface water. -
Physics 114 Tutorial 5: Tension Instructor: Adnan Khan
• Please do not sit alone. Sit next to at least one student. • Please leave rows C, F, J, and M open. Physics 114 Tutorial 5: Tension Instructor: Adnan Khan 5/7/19 1 Blocks connected by a rope q Section 1: Two blocks, A and B, are tied together with a rope of mass M. Block B is being pushed with a constant horizontal force as shown at right. Assume that there is no friction between the blocks and the blocks are moving to the right. 1. Describe the motion of block A, block B, and the rope. 2. Compare the acceleration of block A, block B and the rope. 5/7/19 2 Blocks connected by a rope 2. Compare the accelerations of block A, block B and the rope. A. aA > aR > aB B. aB > aA > aR C. aA > aB > aR D. aB > aR > aA E. aA = aR = aB 5/7/19 3 Blocks connected by a rope 3. Draw a separate free-body diagram for each block and for the rope. Clearly label your forces. 5/7/19 4 Blocks connected by a rope 4. Rank, from largest to smallest, the magnitudes of the horizontal components of the forces on your diagrams. 5/7/19 5 Blocks connected by a very light string q Section 2: The blocks in section 1 are now connected with a very light, flexible, and inextensible string of mass m (m < M). Suppose the hand pushes so the acceleration of the blocks is the same as in section 1. Blocks have same acceleration as with rope 5. -
Estimation of Internal Pressure of Liquids and Liquid Mixtures
Available online at www.ilcpa.pl International Letters of Chemistry, Physics and Astronomy 5 (2012) 1-7 ISSN 2299-3843 Estimation of internal pressure of liquids and liquid mixtures N. Santhi 1, P. Sabarathinam 2, G. Alamelumangai 1, J. Madhumitha 1, M. Emayavaramban 1 1Department of Chemistry, Government Arts College, C.Mutlur, Chidambaram-608102, India 2Retd. Registrar & Head of the Department of Technology, Annamalai University, Annamalainagar-608002, India E-mail address: [email protected] ABSTRACT By combining the van der Waals’ equation of state and the Free Length Theory of Jacobson, a new theoretical model is developed for the prediction of internal pressure of pure liquids and liquid mixtures. It requires only the molar volume data in addition to the ratio of heat capacities and critical temperature. The proposed model is simple, reliably accurate and capable of predicting internal pressure of pure liquids with an average absolute deviation of 4.24% in the predicted internal pressure values compared to those given in literature. The average absolute deviation in the predicted internal pressure values through the proposed model for the five binary liquid mixtures tested varies from 0.29% to 1.9% when compared to those of literature values. Keywords: van der Waals, pressure of liquids, theory of Jacobson, capacity of heat liquids, equation of Srivastava and Berkowitz 1. INTRODUTION The importance of internal pressure in understanding the properties of liquids and the full potential of internal pressure as a structural probe did become apparent with the pioneering work of Hildebrand 1, 2 and the first review of the subject by Richards 3 appeared in 1925.