A Mathematical Approach to Consider Solid Compressibility in the Compression of Pharmaceutical Powders
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Modeling Two Phase Flow Heat Exchangers for Next Generation Aircraft
Wright State University CORE Scholar Browse all Theses and Dissertations Theses and Dissertations 2017 Modeling Two Phase Flow Heat Exchangers for Next Generation Aircraft Hayder Hasan Jaafar Al-sarraf Wright State University Follow this and additional works at: https://corescholar.libraries.wright.edu/etd_all Part of the Mechanical Engineering Commons Repository Citation Al-sarraf, Hayder Hasan Jaafar, "Modeling Two Phase Flow Heat Exchangers for Next Generation Aircraft" (2017). Browse all Theses and Dissertations. 1831. https://corescholar.libraries.wright.edu/etd_all/1831 This Thesis is brought to you for free and open access by the Theses and Dissertations at CORE Scholar. It has been accepted for inclusion in Browse all Theses and Dissertations by an authorized administrator of CORE Scholar. For more information, please contact [email protected]. MODELING TWO PHASE FLOW HEAT EXCHANGERS FOR NEXT GENERATION AIRCRAFT A thesis submitted in partial fulfillment of the requirements for the degree of Master of Science in Mechanical Engineering By HAYDER HASAN JAAFAR AL-SARRAF B.Sc. Mechanical Engineering, Kufa University, 2005 2017 Wright State University WRIGHT STATE UNIVERSITY GRADUATE SCHOOL July 3, 2017 I HEREBY RECOMMEND THAT THE THESIS PREPARED UNDER MY SUPERVISION BY Hayder Hasan Jaafar Al-sarraf Entitled Modeling Two Phase Flow Heat Exchangers for Next Generation Aircraft BE ACCEPTED IN PARTIAL FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF Master of Science in Mechanical Engineering. ________________________________ Rory Roberts, Ph.D. Thesis Director ________________________________ Joseph C. Slater, Ph.D., P.E. Department Chair Committee on Final Examination ______________________________ Rory Roberts, Ph.D. ______________________________ James Menart, Ph.D. ______________________________ Mitch Wolff, Ph.D. -
How Compressible Are Innovation Processes?
1 How Compressible are Innovation Processes? Hamid Ghourchian, Arash Amini, Senior Member, IEEE, and Amin Gohari, Senior Member, IEEE Abstract The sparsity and compressibility of finite-dimensional signals are of great interest in fields such as compressed sensing. The notion of compressibility is also extended to infinite sequences of i.i.d. or ergodic random variables based on the observed error in their nonlinear k-term approximation. In this work, we use the entropy measure to study the compressibility of continuous-domain innovation processes (alternatively known as white noise). Specifically, we define such a measure as the entropy limit of the doubly quantized (time and amplitude) process. This provides a tool to compare the compressibility of various innovation processes. It also allows us to identify an analogue of the concept of “entropy dimension” which was originally defined by R´enyi for random variables. Particular attention is given to stable and impulsive Poisson innovation processes. Here, our results recognize Poisson innovations as the more compressible ones with an entropy measure far below that of stable innovations. While this result departs from the previous knowledge regarding the compressibility of fat-tailed distributions, our entropy measure ranks stable innovations according to their tail decay. Index Terms Compressibility, entropy, impulsive Poisson process, stable innovation, white L´evy noise. I. INTRODUCTION The compressible signal models have been extensively used to represent or approximate various types of data such as audio, image and video signals. The concept of compressibility has been separately studied in information theory and signal processing societies. In information theory, this concept is usually studied via the well-known entropy measure and its variants. -
Chapter 3 3.4-2 the Compressibility Factor Equation of State
Chapter 3 3.4-2 The Compressibility Factor Equation of State The dimensionless compressibility factor, Z, for a gaseous species is defined as the ratio pv Z = (3.4-1) RT If the gas behaves ideally Z = 1. The extent to which Z differs from 1 is a measure of the extent to which the gas is behaving nonideally. The compressibility can be determined from experimental data where Z is plotted versus a dimensionless reduced pressure pR and reduced temperature TR, defined as pR = p/pc and TR = T/Tc In these expressions, pc and Tc denote the critical pressure and temperature, respectively. A generalized compressibility chart of the form Z = f(pR, TR) is shown in Figure 3.4-1 for 10 different gases. The solid lines represent the best curves fitted to the data. Figure 3.4-1 Generalized compressibility chart for various gases10. It can be seen from Figure 3.4-1 that the value of Z tends to unity for all temperatures as pressure approach zero and Z also approaches unity for all pressure at very high temperature. If the p, v, and T data are available in table format or computer software then you should not use the generalized compressibility chart to evaluate p, v, and T since using Z is just another approximation to the real data. 10 Moran, M. J. and Shapiro H. N., Fundamentals of Engineering Thermodynamics, Wiley, 2008, pg. 112 3-19 Example 3.4-2 ---------------------------------------------------------------------------------- A closed, rigid tank filled with water vapor, initially at 20 MPa, 520oC, is cooled until its temperature reaches 400oC. -
A Thermodynamic Theory of Economics
________________________________________________________________________________________________ A Thermodynamic Theory of Economics Final Post Review Version ________________________________________________________________________________________________ John Bryant VOCAT International Ltd, 10 Falconers Field, Harpenden, AL5 3ES, United Kingdom. E-mail: [email protected] Abstract: An analogy between thermodynamic and economic theories and processes is developed further, following a previous paper published by the author in 1982. Economic equivalents are set out concerning the ideal gas equation, the gas constant, pressure, temperature, entropy, work done, specific heat and the 1st and 2nd Laws of Thermodynamics. The law of diminishing marginal utility was derived from thermodynamic first principles. Conditions are set out concerning the relationship of economic processes to entropic gain. A link between the Le Chatelier principle and economic processes is developed, culminating in a derivation of an equation similar in format to that of Cobb Douglas production function, but with an equilibrium constant and a disequilibrium function added to it. A trade cycle is constructed, utilising thermodynamic processes, and equations are derived for cycle efficiency, growth and entropy gain. A thermodynamic model of a money system is set out, and an attempt is made to relate interest rates, the rate of return, money demand and the velocity of circulation to entropy gain. Aspects concerning the measurement of economic value in thermodynamic terms are discussed. Keywords: Thermodynamics, economics, Le Chatelier, entropy, utility, money, equilibrium, value, energy. Publisher/Journal: This paper is the final post review version of a paper submitted to the International Journal of Exergy, published by Inderscience Publishers. Reference: Bryant, J. (2007) ‘A thermodynamic theory of economics’, Int. J. Exergy, Vol 4, No. -
Real Gases – As Opposed to a Perfect Or Ideal Gas – Exhibit Properties That Cannot Be Explained Entirely Using the Ideal Gas Law
Basic principle II Second class Dr. Arkan Jasim Hadi 1. Real gas Real gases – as opposed to a perfect or ideal gas – exhibit properties that cannot be explained entirely using the ideal gas law. To understand the behavior of real gases, the following must be taken into account: compressibility effects; variable specific heat capacity; van der Waals forces; non-equilibrium thermodynamic effects; Issues with molecular dissociation and elementary reactions with variable composition. Critical state and Reduced conditions Critical point: The point at highest temp. (Tc) and Pressure (Pc) at which a pure chemical species can exist in vapour/liquid equilibrium. The point critical is the point at which the liquid and vapour phases are not distinguishable; because of the liquid and vapour having same properties. Reduced properties of a fluid are a set of state variables normalized by the fluid's state properties at its critical point. These dimensionless thermodynamic coordinates, taken together with a substance's compressibility factor, provide the basis for the simplest form of the theorem of corresponding states The reduced pressure is defined as its actual pressure divided by its critical pressure : The reduced temperature of a fluid is its actual temperature, divided by its critical temperature: The reduced specific volume ") of a fluid is computed from the ideal gas law at the substance's critical pressure and temperature: This property is useful when the specific volume and either temperature or pressure are known, in which case the missing third property can be computed directly. 1 Basic principle II Second class Dr. Arkan Jasim Hadi In Kay's method, pseudocritical values for mixtures of gases are calculated on the assumption that each component in the mixture contributes to the pseudocritical value in the same proportion as the mol fraction of that component in the gas. -
Thermodynamics As a Substantive and Formal Theory for the Analysis of Economic and Biological Systems
Thermodynamics as a Substantive and Formal Theory for the Analysis of Economic and Biological Systems The research presented in this thesis was carried out at the Department of Theoretical Life Sciences, Vrije Universiteit Amsterdam, The Netherlands and at the Environment and Energy Section, Instituto Superior T´ecnico, Lisbon, Portugal. VRIJE UNIVERSITEIT THERMODYNAMICS AS A SUBSTANTIVE AND FORMAL THEORY FOR THE ANALYSIS OF ECONOMIC AND BIOLOGICAL SYSTEMS ACADEMISCH PROEFSCHRIFT ter verkrijging van de graad van doctor aan de Vrije Universiteit Amsterdam, op gezag van de rector magnificus prof.dr. L.M. Bouter, in het openbaar te verdedigen ten overstaan van de promotiecommissie van de faculteit der Aard- en Levenswetenschappen op dinsdag 6 februari 2007 om 10.00 uur in de aula van de Instituto Superior T´ecnico Av. Rovisco Pais, n◦1 1049-001 Lisboa door Taniaˆ Alexandra dos Santos Costa e Sousa geboren te Beira, Mozambique promotor: prof.dr. S.A.L.M. Kooijman Contents 1 Introduction 1 2 IsNeoclassicalEconomicsFormallyValid? 9 Published in Ecological Economics 58 (2006): 160-169 2.1 Introduction................................. 10 2.2 IstheFormalismofNeoclassicalEconomicswrong? . ...... 12 2.3 A Unified Formalism for Neoclassical Economics and Equilibrium Ther- modynamics................................. 14 2.4 DiscussingtheFormalism. 19 2.5 Conclusions................................. 21 3 Equilibrium Econophysics 29 Published in Physica A 371 (2006): 492-512 3.1 Introduction................................. 30 3.2 FundamentalEquationandtheEquilibriumState . ...... 31 3.3 DualityFormulation............................. 33 3.4 Reversible, Irreversible and Impossible Processes . .......... 35 3.5 Many-stepProcesses ............................ 36 3.6 LegendreTransforms ............................ 38 3.7 Elasticities.................................. 40 3.8 MaxwellRelations ............................. 43 3.9 StabilityConditions and the Le Chatelier Principle . ......... 45 3.10 EquationsofStateandIntegrability . ..... 47 3.11 FirstOrderPhaseTransitions . -
Compressibility of the Fluid
EPJ Web of Conferences 67, 02048 (2014) DOI: 10.1051/epjconf/20146702048 C Owned by the authors, published by EDP Sciences, 2014 Compressibility of the fluid Jana Jablonská1,a 1 Department of Hydromechanics and Hydraulic Equipment, Faculty of Mechanical Engineering, VŠB-Technical University of Ostrava, 17. listopadu 15, 708 33 Ostrava, Czech republic Abstract. The presence of air in the liquid causes the dynamic system behaviour. When solve to issue of the dynamics we often meet problems of cavitation. Cavitation is an undesirable phenomenon, since it causes a disruption of the surrounding material and material destruction. Cavitation is accompanied by loud sound effects and reduces the efficiency of such pumps, etc. Therefore, it is desirable to model systems in which the cavitation might occur. A typical example is a solution of water hammer. 1 Introduction Fluid density after compression is given by m m In solving dynamics of hydraulic systems we often 0 4 4 (4) encounter the problem with cavitation. Cavitation is an V0 V 1 p 1 p undesirable phenomenon that we are trying to prevent. Cavitation depends on the liquid used in the hydraulic Thereof system. Liquids - hydraulic fluids are typical of its air content. The air in the fluid occurs in two forms - C p S D1 T (5) dissolved and undissolved. Dissolved air according to the 0 E K U literature [4] ia controled by Henry's law, its release is complex and difficult to describe action. If we consider the fluid flow with undissolved air it is a flow of mixture - water – air. 3 Determining the modulus of elasticity of liquid 2 Compressibility of the fluid The modulus of elasticity of water is generally in the literature determines the value of 2.1·109 Pa under normal Compressibility of the fluid is character to shrink in conditions, which corresponds to theory 1 (see Figure 3). -
AJR Ch6 Thermochemistry.Docx Slide 1 Chapter 6
Chapter 6: Thermochemistry (Chemical Energy) (Ch6 in Chang, Ch6 in Jespersen) Energy is defined as the capacity to do work, or transfer heat. Work (w) - force (F) applied through a distance. Force - any kind of push or pull on an object. Chemists define work as directed energy change resulting from a process. The SI unit of work is the Joule 1 J = 1 kg m2/s2 (Also the calorie 1 cal = 4.184 J (exactly); and the Nutritional calorie 1 Cal = 1000 cal = 1 kcal. A calorie is the energy needed to increase the temperature of 1 g of water by 1 °C at standard atmospheric pressure. But since this depends on the atmospheric pressure and the starting temperature, there are several different definitions of the “calorie”). AJR Ch6 Thermochemistry.docx Slide 1 There are many different types of Energy: Radiant Energy is energy that comes from the sun (heating the Earth’s surface and the atmosphere). Thermal Energy is the energy associated with the random motion of atoms and molecules. Chemical Energy is stored within the structural units of chemical substances. It is determined by the type and arrangement of the atoms of the substance. Nuclear Energy is the energy stored within the collection of protons and neutrons of an atom. Kinetic Energy is the energy of motion. Chemists usually relate this to molecular and electronic motion and movement. It depends on the mass (m), and speed (v) of an object. ퟏ ke = mv2 ퟐ Potential Energy is due to the position relative to other objects. It is “stored energy” that results from attraction or repulsion (e.g. -
Entropy Is the Only Finitely Observable Invariant
JOURNAL OF MODERN DYNAMICS WEB SITE: http://www.math.psu.edu/jmd VOLUME 1, NO. 1, 2007, 93–105 ENTROPY IS THE ONLY FINITELY OBSERVABLE INVARIANT DONALD ORNSTEIN AND BENJAMIN WEISS (Communicated by Anatole Katok) ABSTRACT. Our main purpose is to present a surprising new characterization of the Shannon entropy of stationary ergodic processes. We will use two ba- sic concepts: isomorphism of stationary processes and a notion of finite ob- servability, and we will see how one is led, inevitably, to Shannon’s entropy. A function J with values in some metric space, defined on all finite-valued, stationary, ergodic processes is said to be finitely observable (FO) if there is a sequence of functions Sn(x1,x2,...,xn ) that for all processes X converges to X ∞ X J( ) for almost every realization x1 of . It is called an invariant if it re- turns the same value for isomorphic processes. We show that any finitely ob- servable invariant is necessarily a continuous function of the entropy. Several extensions of this result will also be given. 1. INTRODUCTION One of the central concepts in probability is the entropy of a process. It was first introduced in information theory by C. Shannon [S] as a measure of the av- erage informational content of stationary stochastic processes andwas then was carried over by A. Kolmogorov [K] to measure-preserving dynamical systems, and ever since it and various related invariants such as topological entropy have played a major role in the theory of dynamical systems. Our main purpose is to present a surprising new characterization of this in- variant. -
Thermodynamic Properties of Molecular Oxygen
NATIONAL BUREAU OF STANDARDS REPORT 2611 THERMODYNAMIC PROPERTIES OF MOLECULAR OXYGEN tv Harold ¥, Woolley Themodynamics Section Division of Heat and Power U. S. DEPARTMENT OF COMMERCE NATIONAL BUREAU OF STANDARDS U. S. DEPARTMENT OF COMMERCE Sinclair Weeks, Secretary NATIONAL BUREAU OF STANDARDS A. V. Astin, Director THE NATIONAL BUREAU OF STANDARDS The scope of activities of the National Bureau of Standards is suggested in the following listing of the divisions and sections engaged in technical work. In general, each section is engaged in special- ized research, development, and engineering in the field indicated by its title. A brief description of the activities, and of the resultant reports and publications, appears on the inside of the back cover of this report. Electricity. Resistance Measurements. Inductance and Capacitance. Electrical Instruments. Magnetic Measurements. Applied Electricity. Electrochemistry. Optics and Metrology. Photometry and Colorimetry. Optical Instruments. Photographic Technology. Length. Gage. Heat and Power. Temperature Measurements. Thermodynamics. Cryogenics. Engines and Lubrication. Engine Fuels. Cryogenic Engineering. Atomic and Radiation Physics. Spectroscopy. Radiometry. Mass Spectrometry. Solid State Physics. Electron Physics. Atomic Physics. Neutron Measurements. Infrared Spectroscopy. Nuclear Physics. Radioactivity. X-Rays. Betatron. Nucleonic Instrumentation. Radio- logical Equipment. Atomic Energy Commission Instruments Branch. Chemistry. Organic Coatings. Surface Cheipistry. Organic Chemistry. -
Optimal Design of a Hydro-Mechanical Transmission Power Split Hybrid Hydraulic Bus
Optimal Design of a Hydro-Mechanical Transmission Power Split Hybrid Hydraulic Bus A dissertation SUBMITTED TO THE DEPARTMENT OF MECHANICAL ENGINEERING, UNIVERSITY OF MINNESOTA BY Muhammad Iftishah Ramdan IN PARTIAL FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF DOCTOR OF PHILOSOPHY Adviser: Professor Kim A. Stelson December 2013 Copyright ©Muhammad Iftishah Ramdan. All rights reserved. Acknowledgements First and foremost, I would like to express my deepest gratitude to Professor Kim A. Stelson for his guidance and patience during his years as my adviser. I am also grateful to my sponsors, Malaysian Ministry of Higher Education (MOHE) and University of Science, Malaysia (USM), for their financial support during my graduate studies. I would like to express my sincere appreciation to my entire family - my wife, my mother, and siblings, for their endless moral support and for always believing in me. i Dedication This thesis is dedicated to my father who succumbed to COPD, caused in part by the air pollution in Malaysia. I hope my work could be one of the steps towards improving the environment and the public health situation both in my native country and abroad. ii Abstract This research finds the optimal power-split drive train for hybrid hydraulic city bus. The research approaches the optimization problem by studying the characteristics of possible configurations offered by the power-split architecture. The critical speed ratio ( ) is ͍-$/ introduced in this research to represent power-split configurations and consequently simplifies the optimal configuration search process. This methodology allows the research to find the optimal configurations among the more complicated dual-staged power-split architecture. -
Advanced Process Manager Control Functions and Algorithms
Advanced Process Manager Control Functions and Algorithms AP09-600 Implementation Advanced Process Manager - 1 Advanced Process Manager Control Functions and Algorithms AP09-600 Release 650 12/03 Notices and Trademarks © Copyright 2002 and 2003 by Honeywell Inc. Revision 05 – December 5, 2003 While this information is presented in good faith and believed to be accurate, Honeywell disclaims the implied warranties of merchantability and fitness for a particular purpose and makes no express warranties except as may be stated in its written agreement with and for its customer. In no event is Honeywell liable to anyone for any indirect, special or consequential damages. The information and specifications in this document are subject to change without notice. TotalPlant and TDC 3000 are U. S. registered trademarks of Honeywell Inc. Other brand or product names are trademarks of their respective owners. Contacts World Wide Web The following Honeywell Web sites may be of interest to Industry Solutions customers. Honeywell Organization WWW Address (URL) Corporate http://www.honeywell.com Industry Solutions http://www.acs.honeywell.com International http://content.honeywell.com/global/ Telephone Contact us by telephone at the numbers listed below. Organization Phone Number United States and Honeywell International Inc. 1-800-343-0228 Sales Canada Industry Solutions 1-800-525-7439 Service 1-800-822-7673 Technical Support Asia Pacific Honeywell Asia Pacific Inc. (852) 23 31 9133 Hong Kong Europe Honeywell PACE [32-2] 728-2711 Brussels, Belgium Latin America Honeywell International Inc. (954) 845-2600 Sunrise, Florida U.S.A. Honeywell International Process Solutions 2500 West Union Hills Drive Phoenix, AZ 85027 1-800 343-0228 About This Publication This publication supports TotalPlant® Solution (TPS) system network Release 640.