Thermodynamic equations of state of polymers and conversion processing

Size: px
Start display at page:

Download "Thermodynamic equations of state of polymers and conversion processing"

Transcription

1 Polimery, No.,,. 66 hermodynamic equations of state of olymers and conversion rocessing B. Kowalska Selected from International Polymer Science and echnology, 9, No.,, reference P //66; transl. serial no ranslation submitted by E.A. Inglis hermal rocesses, in addition to rheological rocesses, condition the behaviour of a lastic in rocessing equiment and the roerties and structure of the roducts. he thermal state of a lastic is determined by the following factors: the ressure, secific volume and temerature. An imortant consideration during rocessing is the deendence of the secific volume on temerature at atmosheric ressure (Figure ). he relationshi between the ressure, volume and temerature is called the thermodynamic equation of state, or more simly the equation of state. Under equilibrium conditions the equation of state of a single-hase system is given by the equation () (ref. ): F (,, v) = () he simlest thermodynamic equation of state is the equation for a erfect gas in the form = nr () where R is the universal gas constant, [R = 84 J/ (kmol.k], and n is the number of moles of the substance. his equation assumes that the gas molecules are oint masses and hence have no secific volume, and do not interact with each other outside the moment of elastic imact. However, the molecules of real gases do have a secific volume, hence the effective accessible volume for movements of the molecules is less than the total volume of the system. he mutual attraction of the molecules causes a reduction in ressure, so that the molecules not interacting with each other move to the walls of the container in which the gas is located. In order to allow for the secific volume of molecules Van der Waals introduced a correction for the volume of the gas and reduced it to an active value, by subtracting the so-called co-volume b, equal to the sum of elementary sheres around all of the molecules. In the case of sherical molecules b is equal to four times their volume. he correction for ressure, called the cohesion ressure is according to Van der Waals roortional both to the number of attracted and attracting molecules, and thus is roortional to the square of the gas density ρ (ref. ); this relationshi is shown in equation (): a = aρ = () v where a is a coefficient of roortionality indeendent of the arameters of state. Because of this instead of equation () in its simlest form ( = R) we obtain: a + ( b) = R (4) his is an algebraic equation of the third degree with resect to ; after transformation it takes the form: b + R a ab + = In the analysis of hysical henomena it is desirable to emloy dimensionless magnitudes since in this way we can avoid the effect of the system of units adoted. For the thermodynamic dimensionless arameters we can take the ratios of arameters to their values in the critical state (also referred to as the reducing arameters, indicated below by an asterisk). In this way we obtain reduced arameters (indicated by the symbol ~) (refs. 4 and ): () /76 International Polymer Science and echnology, Vol. 9, No. 7,

2 ; ; = = = On introducing the reduced arameters into the Van der Waals equation we obtain the reduced equation of state in dimensionless form containing only universal constants (without material constants): (6) + ( ) = 8 (7) Equation (7) itself and any other equation of state in dimensionless form is a criterion of thermodynamic similarity; it is called an equation of corresonding states (ref. ). Different substances are in corresonding states when their reduced arameters have the same numerical values. he critical oints of each substance are corresonding states. From this it emerges that if any two fluids have two identical reduced arameters, then their remaining reduced arameter has the same value. he use of the rincile of corresonding states in technical calculations is of great imortance. According to the above rincile the relationshi ( ) = (8) F,, is the most universal equation of state for real gases and liquids. However, it is found from exerimental results (ref. ) that the state of substances being comared cannot always be described using only three reduced arameters. he theory has therefore been exanded by introducing a fourth arameter, the so-called determining criterion A. hus: ( ) = (9) F,,, A he value of A, which characterises the individual roerties of bodies, can be defined in various ways. Most commonly the criterion is the coefficient of comression of a substance at the critical oint (ref. ): Z = R () At a later stage we shall show how the -- relationshis can be used to further discover the henomena occurring during rocessing and to determine the connections between rocessing factors. USE OF HE HERMODYNAMIC EQUAION OF SAE IN HE CONVERSION OF POLYMERS he use of the equation of state in the conversion of olymers will be characterised using as an examle one of the commonest rocessing methods, namely injection moulding. he main factors in injection moulding are temerature, ressure and time. hese may vary widely. Variable external ressure affects e.g. the density of the lastic and the shae and dimensions of the moulding. By using a redetermined rogram of change in external ressure many roerties of the moulding are otimised (refs. 6 ). Simultaneous recording of ressure and temerature at the same site in the moulding cavity makes it ossible to lot their changes on a -- grah (Figures and ). he theoretical curve of the rocess (Figure ) marks out simle lines: the isotherm of ressure A, the isobar corresonding to the ressure hase B and the isochore of cooling C (refs. and ). Figure. -n- grahs reresenting a theoretical injection moulding cycle for olystyrene; isobars corresonding to ressure (in MPa): a., b, c 4, d 6, f 6 (for further exlanations see test) (refs. 7 and 8) Figure. -n- grah of a real injection moulding cycle for olystyrene; for meaning of isobar symbols see Figure ) (refs. 7 and 8) International Polymer Science and echnology, Vol. 9, No. 7, /77

3 At oint on the isotherm A the lastic reaches the ressure sensor. Point denotes comlete volume filling of the moulding cavity under low ressure conditions. Raid comression of the liquid lastic in the cavity is shown by lines. he lastic comressed to a ressure with a value defined by the isobar assing through oint and cooled remains fixed at the same isobar until it reaches a temerature at which solidification of the lastic at the narrowest oint occurs (oint ). his is a very imortant oint in the injection moulding rocess, which goes on sontaneously to the stage when he ressure of the lastic reaches a value defined by the isobar as. MPa (oint 4). Further cooling of the lastic causes a decrease in its volume and hence the occurrence of rocessing shrinkage. he actual curve of the injection moulding rocess (Figure ) deviated from the theoretical assumtions. Obtaining a constant value for shrinkage ( s ) is difficult because of the variation in osition of the oint where the lastic solidifies at the narrow oint and because of later uncontrolled changes in the secific volume (ref. ). he -- relationshi can be used to analyse the rocesses taking lace in the moulding cavity during different tyes of injection moulding, such as injectioncomression moulding (refs. and 4). his method of moulding has come to be used for making high-quality mouldings (e.g. comonents of otical devices, CDs). he volume rocessing shrinkage of the moulding when cooled in a tightly closed mould is comensated by a reduction in the dimensions of the mould cavity during the comression hase. his rocess requires two-stage closing of the mould and an additional comression force. he injection and comression hase of the mould are shown in Figure. he rocessing shrinkage of the mouldings accomanying comression can be determined using -- grahs (Figure 4). Figure 4. -n- grah for injection-comression moulding of olystyrene; designation of isobars as in Figure (for further exlanations see test) (ref. 9) Point in Figure 4 corresonds to the filling of the cavity. During flow of the lastic a slight ressure is maintained which is just higher than atmosheric ressure (oint ) until the mould is sontaneously sealed (oint ). hen the volume of the mould cavity is reduced as a result of the ressure, which causes a rise in ressure in the mould (oint 4). he conclusion of cooling of the moulding (oint ) occurs at the isobar corresonding to atmosheric ressure. A small amount of rocessing shrinkage ( s ) occurs on oening the mould and cooling the moulding to ambient temerature. An imortant arameter is the time of delay in comression t determined from the -- grah. he end of comression (oint ) should occur when the mould is sealed, otherwise the lastic may ass through into the runner or further, in the direction of the nozzle. Usually the relations between ressure, secific volume and temerature of the olymers are determined exerimentally. We can also use for this urose mathematical equations (theoretical and exerimental) which are an extension of the thermodynamic equation of state. HEORY OF HEOREICAL EQUAIONS he theoretical equations are based mainly on the equation known from statistical mechanics relating the ressure to secific volume and temerature (ref. ): ln Z = k r () Figure. Diagram of injection-comression moulding rocess: a injection hase; b comression hase (s comression ga comensating for volume contraction) (ref. 9) where k is the Boltzmann constant and Z is a distribution function defined at the atomic level. Direct determination of the distribution function is very difficult, requiring certain assumtions regarding the structure of the macromolecules and intermolecular forces. /78 International Polymer Science and echnology, Vol. 9, No. 7,

4 HE SIMHA-SOMCYNSKY EQUAION Simha and Somcynsky (ref. 6) modified the cellular model roosed by Lennard-Jones and Devonshire (ref. 7). hey defined the magnitude y which is indeendent of temerature, taking the volume of free saces ( holes ) in the system as (- y). Simha and Somcynsky s hole theory made it ossible to define equations describing the reduced variables. he reducing variables, and characterising each olymer were defined as follows (refs. 8 ): he exression c/s is the so-called coefficient of elasticity which characterises the system. he results obtained with different values of this coefficient coincide, hence it is usually assumed that c/s =. P. Zoller (ref. ) determined the reducing arameters of PFE in the liquid state using equations () and (6). he solution of these equations when = allows us to determine the theoretical isobar corresonding to atmosheric ressure as a function of the reduced temerature (Figure ). N A = Ns = M ( z ) se = ck () () ( z ) e = (4) where ' is the volume of a macromolecular segment, N is the number of macromolecules of the olymer, N A is the Avogadro number, M is the molecular weight of a segment of the macromolecule, e is the minimum intersegmental otential energy, s is the number of segments in the macromolecule, z is the coordination number, k is Boltzmann s constant, and c is the number of external degrees of freedom of the macromolecule. he equation of state for the reduced variables takes the form: = 6 yy ( ) [ ( )]. y. 4 y + y... ( ) () According to the Simha-Somcynsky theory y defines the units of the quasi-crystalline network occuied by segments of the macromolecules; hence (-y) is the region of free saces between the segments and thus when s equation () can be written in the form: [ ( )] = s + y ln y c [ ] y ( y ). 49. ( y ) 6 6 yy y y 6 + ( ) (6) Figure. Isobar of = for PFE determined exerimentally in the molten state (solid oints) and suerimosed on the theoretical ( = ) isobar (continuous line) (ref. 7) he exerimental oints of the relationshi log vs. log are dislaced arallel to the axis according to the method of suerimosition, until satisfactory results are obtained. Using this method we can use Figure to determine the reducing arameters: = 796K and = m /kg. he reducing arameter of ressure was determined using the Simha-Somcynsky theory for each value of reduced ressure ISING S EQUAION Most equations of state of olymers use a cellular model that requires searation of the internal and external degrees of freedom. he external degrees of freedom attributed to the chain segment of the olymer are lower than in the case of a low-molecular comound. Since Ising s model does not involve a cellular model, there is no need to searate the internal and external degrees of freedom (ref. ). Ising s equation relating to the reduced arameters of olymers in the liquid state takes the form: ln + + ( )+ r = (7) International Polymer Science and echnology, Vol. 9, No. 7, /79

5 where r is the number of units in the crystalline network occuied by the rth mer. he reducing arameters can be related to the molecular weight by the equation: Ising s equation aroximates to the exerimental data much more closely than the comlex equations based on a cellular model. In addition, it can describe the roerties of fluids with a low molecular weight. R M ρ = (8) r Since the arameter r aears in the reduced equation of state (7), the basic requirement of selfsimilar states is not fulfilled. However, for a olymer in the liquid state the value r, and equation (7) reduces to the form: [ ] = ρ + + ln ( ρ )+ ρ (9) hus olymers in the liquid state with a corresondingly high molecular weight must fulfil the basic requirement of corresonding states. his was confirmed exerimentally by I.C. Sanchez and R.H. Lacombe (ref. ). In the grah (Figure 6) it can be seen that in the case of the ten olymers studied the rincile of corresonding states is fulfilled over a wide range of temerature and ressure. he lines are theoretical isobars calculated from equation (9) on the basis of the reduced ressure and exerimental density measurements corresondingly reduced by the reducing arameters. he maximum error in the density calculations is.%, and the average is.%. Exerimental errors in the determination of the density are in the range..%. PASINE AND WARFIELD S EQUAION A three-arameter equation of state exressed with the use of reduced variables was roosed by D.J. Pastine and R.W. Warfield (ref. ).his was designed for olymers in the liquid state on the basis of the theory of a vibrating chain in a rigid cylinder. It can be reresented by the general relationshi: ( ) = ( )+ ( ), A () where A is a volume function, is the internal ressure, deendent on the internal energy of the olymer. Using the Simha-Somcynsky relationshi under conditions of atmosheric ressure this equation of state can be rewritten in the form: ( ) = ( )+ ln, ln, () In equation () the values (,) later referred to as and reresent the coefficients of this equation. Assuming that f ( ) ( ) = A () and using equations () and () we obtain the relationshi: ( ) ( ), f = ln () in which f() has the ressure dimension. Pastine and Warfield studied olymers in the ressure range MPa, at a temerature exceeding (u to C) the temerature of the corresonding hase change of the given olymer. From exerimental data they determined f() in the form: Figure 6. Grahical reresentation of the rincile of corresonding states for olymers. he lines are theoretical isobars calculated from equation (9) for various values of :.,., (ref. 8). ( ) = f B (4) where B is a arameter showing the ressure magnitude. /8 International Polymer Science and echnology, Vol. 9, No. 7,

6 he above-mentioned authors defined B, and as reducing arameters, determining them by extraolation to a temerature of C and a ressure of zero. Substituting f() into equation of state () we obtain: ln B = () Introducing the reduced variables = / B, = /, = / simlifies equation () to the form: = ln (6) which fulfils the rincile of corresonding states. In order to comare the values obtained from equation (6) with the exerimental data (ref. ), first of all the secific volume and temerature by substituting into equation () =. hen the arameter B was determined, lotting the relationshi = f( / ) for a constant secific volume. he reducing arameters were established by comaring the values of the secific volumes found exerimentally with the values calculated from equation (6). he results for PE-HD in the form of grahs of the theoretical and exerimental isotherms are shown in Figure 7. Corresonding results for the isobars are shown in Figure 8. In both these cases the accuracy of comarison between the exerimental and theoretical data is about. cm /g. Figure 8. HDPE isobars corresonding to ressure (in MPa) : a., b 4, c 8, d, e 6, f (the circles indicate exerimental data; the lines are theoretical, determined using equation (6) (ref. 9) WHIAKER AND GRISKEY S EQUAION his equation was evolved on the basis of the theory of corresonding states (ref. 4). Considering the coefficient of comression: Z = (7) R it was observed that the relationshi between Z and the reduced temerature (/ g ) shows a set of corresonding curves (dislaced arallel to themselves) determined for different olymers under atmosheric ressure (Figure 9). Figure 7. HDPE isotherms corresonding to temerature: a 4. C, b.9 C, c 6.4 C, d 7. C, e 8.9 C, f 89.6 C, g 99.7 C (the circles denote exerimental data, and the continuous line are theoretical, determined using equation (6) (ref. 9) Figure 9.Grah of comressibility coefficient (Z) vs. reduced temerature (/ g ) at atmosheric ressure for different olymers (ref. ) International Polymer Science and echnology, Vol. 9, No. 7, /8

7 From the data in Figure 9 we obtained the following general relationshi between the temerature ( in K), ressure ( in Pa) and secific volume (V in m ): V. =. 94 ρ n g m+ R (8) where ρ is the density at C and ressure. MPa, g is the glass transition temerature, R is the universal gas constant in J/(kg.K), and m and n are equation arameters. he mean error of the data calculated from equation (8) and the exerimental data is %. It is only in the melting region of the olymers that equation (8) does not corresond to the exerimental data there is a discontinuity in the case of all of the studied olymers having a clearly defined melting range. Finally, on differentiating the Whitaker-Griskey equation and taking definite values of the constants and exonents, we get the relationshi: x V K y = (9) g in which ω is a constant value for one kilogram of the olymer (m /kg). Substituting in equation () the exression R M = R () where R' is the individual gas constant exressed in J/ (kg.k), we obtain a thermodynamic equation of state of olymers in the following form: ( + πi )( ω ) = R (4) Equations () and (4) are extremely imortant as regards measurement ossibilities. he Sencer-Gilmore model is of course one of the oldest models, but it still continues to be used in studies of olymers (refs. 7 ). ait s equation ait s equation resents the change in secific volume along the isotherm as a function of two variable arameters B() and C() (refs. 9 and ): where x and y are exonents reresenting ressure functions, K is a function of density at C and at ressure of. MPa (refs. 4).,, Cln ( ) = ( ) + ( ) B () REVIEW OF EXPERIMENAL EQUAIONS he Sencer-Gilmore equation A thermodynamic equation of state of olymers arising from the Van der Waals equation was roosed by Sencer and Gilmore (refs. ) in the form: ( + πi) ( M ω M) = R () where is the external absolute ressure, π i is the internal ressure (cohesion ressure) taken as being indeendent of the volume, M is the secific volume of a single kilomole of olymer under ressure and at temerature, ω M is a coefficient reresenting the constant volume of the olymer macromolecules at a temerature of absolute zero. If we consider the relation between the secific volume for one kilomole, or M = M () where M is the molar mass in g/mol, then equation () takes the form: ( + πi ) ω ( ) = R M () where (, ) is the secific volume at ressure and temerature, C is a universal constant equal to.984, and B() is a arameter defined by the relation ( ) = ( ) B B ex B (6) where B and B are characteristic constants of the given olymer. he volume under atmosheric ressure denoted by (,) and determined by extraolation can be reresented as a olynomial at a temerature < m ( ) = (7), A A A A... or as an exonent, where > m ( ) = ( ) (8), ex α where is the secific volume at atmosheric ressure, α is the coefficient of volume exansion at atmosheric ressure. he authors of ref. 9 have determined the arameter B of several olymers in the liquid and solid states. able shows average values of this arameter in a temerature corresonding to the liquid state of the selected olymers. /8 International Polymer Science and echnology, Vol. 9, No. 7,

8 able. Exerimental and theoretical values of arameter B of olymers in the liquid state (ref. 9) P olymer and corresonding theoretical equation, C PS - B = 4 ex (-4.4 x ) PMMA - B = 8 ex (-6.7 x ) PVC - B = ex (-.6 x ) Exerimental Parameter B, MPa heoretical he maximum deviations between the theoretical calculations in able and the exerimental results for PS, PMMA and PVC are.96%,.% and.8% resectively. CONCLUSION here are many mathematical forms of the thermodynamic equation of state of olymers. he reason for this variety is the various aroaches to the roblem and its solution. Also, an equation of this kind must corresond to the criteria listed below, which are difficult to meet at the same time (ref. 4): - it must be valid over a wide range of ressure and temeratures; - its mathematical form must be generalised so that it can be used for many olymers differing in their roerties and states of aggregation; - it must be relatively simle and easy to use; - it must also enable the calculation of thermodynamic relationshis of the olymer when only hysical roerties that are relatively easy to measure are known, such as the glass transition temerature or melting oint at atmosheric ressure and density at C and under atmosheric ressure. Equations fulfilling all these criteria usually relate to articular grous of olymers either in the solid or liquid state, but it is rarely ossible to describe the behaviour of a articular olymer in both these states. For this reason the existing equations are continually modified and imroved in order to obtain the most universal models. In the field of rocessing use has been made of exerimental equations, mainly Gilmore and Sencer s equation and ait s equation, in which the constants have been emloyed for he conditions of a articular conversion rocess. he relations between these conditions are highly comlex, and for this reason the use of the equations continues to be restricted, and the literature covering these roblems is inadequate. In conversion rocesses it is also imortant to know the derivatives of the secific volume as a function of ressure and temerature. Using the first derivative we can determine the coefficients of volume exansion and the coefficients of comressibility which lay an imortant art in the designing of dimensions of injection mouldings. he exerimental equations of state on differentiation determine the values of these coefficients. Examination of the literature shows among other things the continuously oor knowledge of the relationshi between equations of state and the fundamentals of highmolecular lastics rocessing. In connection with this results will be resented in another article of our own investigations into the effect of cooling of injection mouldings on the thermodynamic equation of state. REFERENCES. R. Sikora Fundamentals of rocessing of highmolecular lastics, Lublin Polytechnic, 99,.8.. J. Szarawara, Alied chemical International Polymer Science and echnology, Vol. 9, No. 7, /8

9 thermodynamics, WNR, Warsaw 997,.7... Haut, Fundamentals of thermodynamics, Krakow 98,.. 4. E. Kalinowski, hermodynamics, Wroclaw Poolytechnic, Wroclaw 994,... J. Madejski, Engineering thermodynamics, Rzeszow Polytechnic,,.. 6. A. Smorawinski, Injection moulding technology, WN, Warsaw 984, F. Johannaber, Plastic machine guide, Carl Hanser Verlag, Munich-Vienna 99,.6; F. Johannaber, Injection moulding machines a user s guide, Warsaw, B. Lackowski, Mechanik,, 98, H. Zawistowski, Reorts from the National echnical Conference Injection moulding and extrusion technology, Czestochowa, 988,... Ideas for rocessing otimisation, Battenfeld,.9.. H. Zawistowski, Mechanik, 6, 99,... D. Rheinfeld and R. Jensen, Kunststoffe, 6, 97, W. Knae and A. Laml, Kunststoffe, 74, 984, B. Friedrichs et al., Kunststoffe, 8, 99,.8.. L.C. ucker, Fundamentals of comuter modeling for olymer rocessing, Carl Hanser Verlag, Munich-Vienna-New York 989, R. Simha and. Somcynski, Macromolecules,, 969, J.E. Lennard-Jones and A.F. Devonshire, Proc. Roy. Soc., A6, 97,.. 8. J.E. McKinney and R. Simha, J. Res., 8, 977, R. Simha et al., Kolloid-Zeitschrift und Zeitschrift fur Polymere,, 97,.4.. P. Zoller, J. Al. Polym. Sci.,, 979,... P. Zoller, J. Al. Polym. Sci.,, 978,.6.. I.C. Sanchez and R.H. Lacombe, Polym. Lett. Ed.,, 977,.7.. B. Hartmann and A.M. Haque, J.Al. Polym. Sci.,, 98,.. 4. K. Rao and R.G. Griskey, J. Al. Polym. Sci., 7, 97,.9.. R.S. Sencer and G.D. Gilmore, J. Al. Phys.,, 949,.. 6. E. Bernhardt (Ed.), Processing of thermolastics materials, Reinhold, New York X. Guo et al., Polym. Engng Sci., 9, 999, J.W. Sikora and B. Kowalska, Archiwum nauki o materialach, 9, 998,.. 9. E. Bociaga and B. Samujlo, he influence of constructional solutions of the injection moulding runner system on the thermal equation of state of olyethylene, Polymer Processing Society, Euroe/Africa Regional Meeting, Zlin, Czech Reublic,... E. Bociaga and B. Samujlo, Archiwum nauki o materialach (in the ress).. B. Kowalska et al., he influence of aluminium hydroxide on the form of Sencer and Gilmore thermodynamic equation of state for olymers, Polymer Processing Society, th Annual Meeting, s-hertogenbosch, Holland 999,.4.. R. Sikora et al., Seed of the screw and thermal equation of state of autothermally extruded olyethylene : the Polymer Processing Society, 4 th Annual Meeting, Yokohama, Jaan 998,.. (Received 9//) /84 International Polymer Science and echnology, Vol. 9, No. 7,

Phase transition. Asaf Pe er Background

Phase transition. Asaf Pe er Background Phase transition Asaf Pe er 1 November 18, 2013 1. Background A hase is a region of sace, throughout which all hysical roerties (density, magnetization, etc.) of a material (or thermodynamic system) are

More information

dn i where we have used the Gibbs equation for the Gibbs energy and the definition of chemical potential

dn i where we have used the Gibbs equation for the Gibbs energy and the definition of chemical potential Chem 467 Sulement to Lectures 33 Phase Equilibrium Chemical Potential Revisited We introduced the chemical otential as the conjugate variable to amount. Briefly reviewing, the total Gibbs energy of a system

More information

FUGACITY. It is simply a measure of molar Gibbs energy of a real gas.

FUGACITY. It is simply a measure of molar Gibbs energy of a real gas. FUGACITY It is simly a measure of molar Gibbs energy of a real gas. Modifying the simle equation for the chemical otential of an ideal gas by introducing the concet of a fugacity (f). The fugacity is an

More information

HEAT, WORK, AND THE FIRST LAW OF THERMODYNAMICS

HEAT, WORK, AND THE FIRST LAW OF THERMODYNAMICS HET, ORK, ND THE FIRST L OF THERMODYNMIS 8 EXERISES Section 8. The First Law of Thermodynamics 5. INTERPRET e identify the system as the water in the insulated container. The roblem involves calculating

More information

THERMODYNAMICS. Prepared by Sibaprasad Maity Asst. Prof. in Chemistry For any queries contact at

THERMODYNAMICS. Prepared by Sibaprasad Maity Asst. Prof. in Chemistry For any queries contact at HERMODYNAMIS reared by Sibarasad Maity Asst. rof. in hemistry For any queries contact at 943445393 he word thermo-dynamic, used first by illiam homson (later Lord Kelvin), has Greek origin, and is translated

More information

THE FIRST LAW OF THERMODYNAMICS

THE FIRST LAW OF THERMODYNAMICS THE FIRST LA OF THERMODYNAMIS 9 9 (a) IDENTIFY and SET UP: The ressure is constant and the volume increases (b) = d Figure 9 Since is constant, = d = ( ) The -diagram is sketched in Figure 9 The roblem

More information

The Second Law: The Machinery

The Second Law: The Machinery The Second Law: The Machinery Chater 5 of Atkins: The Second Law: The Concets Sections 3.7-3.9 8th Ed, 3.3 9th Ed; 3.4 10 Ed.; 3E 11th Ed. Combining First and Second Laws Proerties of the Internal Energy

More information

Phase Equilibrium Calculations by Equation of State v2

Phase Equilibrium Calculations by Equation of State v2 Bulletin of Research Center for Comuting and Multimedia Studies, Hosei University, 7 (3) Published online (htt://hdl.handle.net/4/89) Phase Equilibrium Calculations by Equation of State v Yosuke KATAOKA

More information

whether a process will be spontaneous, it is necessary to know the entropy change in both the

whether a process will be spontaneous, it is necessary to know the entropy change in both the 93 Lecture 16 he entroy is a lovely function because it is all we need to know in order to redict whether a rocess will be sontaneous. However, it is often inconvenient to use, because to redict whether

More information

PHYS1001 PHYSICS 1 REGULAR Module 2 Thermal Physics Chapter 17 First Law of Thermodynamics

PHYS1001 PHYSICS 1 REGULAR Module 2 Thermal Physics Chapter 17 First Law of Thermodynamics PHYS1001 PHYSICS 1 REGULAR Module Thermal Physics Chater 17 First Law of Thermodynamics References: 17.1 to 17.9 Examles: 17.1 to 17.7 Checklist Thermodynamic system collection of objects and fields. If

More information

not to be republished NCERT STATES OF MATTER UNIT 5 INTRODUCTION

not to be republished NCERT STATES OF MATTER UNIT 5 INTRODUCTION 32 CHEMISRY UNI 5 SAES OF MAER After studying this unit you will be able to exlain the existence of different states of matter in terms of balance between intermolecular forces and thermal energy of articles;

More information

δq T = nr ln(v B/V A )

δq T = nr ln(v B/V A ) hysical Chemistry 007 Homework assignment, solutions roblem 1: An ideal gas undergoes the following reversible, cyclic rocess It first exands isothermally from state A to state B It is then comressed adiabatically

More information

Churilova Maria Saint-Petersburg State Polytechnical University Department of Applied Mathematics

Churilova Maria Saint-Petersburg State Polytechnical University Department of Applied Mathematics Churilova Maria Saint-Petersburg State Polytechnical University Deartment of Alied Mathematics Technology of EHIS (staming) alied to roduction of automotive arts The roblem described in this reort originated

More information

602 ZHANG Zhi and CHEN Li-Rong Vol Gibbs Free Energy From the thermodynamics, the Gibbs free energy of the system can be written as G = U ; TS +

602 ZHANG Zhi and CHEN Li-Rong Vol Gibbs Free Energy From the thermodynamics, the Gibbs free energy of the system can be written as G = U ; TS + Commun. Theor. Phys. (Beijing, China) 37 (2002) 601{606 c International Academic Publishers Vol. 37, No. 5, May 15, 2002 The 2D Alternative Binary L J System: Solid-Liquid Phase Diagram ZHANG Zhi and CHEN

More information

Chapter 1 Fundamentals

Chapter 1 Fundamentals Chater Fundamentals. Overview of Thermodynamics Industrial Revolution brought in large scale automation of many tedious tasks which were earlier being erformed through manual or animal labour. Inventors

More information

Compressible Flow Introduction. Afshin J. Ghajar

Compressible Flow Introduction. Afshin J. Ghajar 36 Comressible Flow Afshin J. Ghajar Oklahoma State University 36. Introduction...36-36. he Mach Number and Flow Regimes...36-36.3 Ideal Gas Relations...36-36.4 Isentroic Flow Relations...36-4 36.5 Stagnation

More information

arxiv:cond-mat/ v2 25 Sep 2002

arxiv:cond-mat/ v2 25 Sep 2002 Energy fluctuations at the multicritical oint in two-dimensional sin glasses arxiv:cond-mat/0207694 v2 25 Se 2002 1. Introduction Hidetoshi Nishimori, Cyril Falvo and Yukiyasu Ozeki Deartment of Physics,

More information

CFD AS A DESIGN TOOL FOR FLUID POWER COMPONENTS

CFD AS A DESIGN TOOL FOR FLUID POWER COMPONENTS CFD AS A DESIGN TOOL FOR FLUID POWER COMPONENTS M. BORGHI - M. MILANI Diartimento di Scienze dell Ingegneria Università degli Studi di Modena Via Cami, 213/b 41100 Modena E-mail: borghi@omero.dsi.unimo.it

More information

Pressure-sensitivity Effects on Toughness Measurements of Compact Tension Specimens for Strain-hardening Solids

Pressure-sensitivity Effects on Toughness Measurements of Compact Tension Specimens for Strain-hardening Solids American Journal of Alied Sciences (9): 19-195, 5 ISSN 1546-939 5 Science Publications Pressure-sensitivity Effects on Toughness Measurements of Comact Tension Secimens for Strain-hardening Solids Abdulhamid

More information

ANALYTICAL MODEL FOR THE BYPASS VALVE IN A LOOP HEAT PIPE

ANALYTICAL MODEL FOR THE BYPASS VALVE IN A LOOP HEAT PIPE ANALYTICAL MODEL FOR THE BYPASS ALE IN A LOOP HEAT PIPE Michel Seetjens & Camilo Rindt Laboratory for Energy Technology Mechanical Engineering Deartment Eindhoven University of Technology The Netherlands

More information

Homogeneous and Inhomogeneous Model for Flow and Heat Transfer in Porous Materials as High Temperature Solar Air Receivers

Homogeneous and Inhomogeneous Model for Flow and Heat Transfer in Porous Materials as High Temperature Solar Air Receivers Excert from the roceedings of the COMSOL Conference 1 aris Homogeneous and Inhomogeneous Model for Flow and Heat ransfer in orous Materials as High emerature Solar Air Receivers Olena Smirnova 1 *, homas

More information

SELF-SIMILAR FLOW UNDER THE ACTION OF MONOCHROMATIC RADIATION BEHIND A STRONG CYLINDRICAL SHOCK WAVE IN A NON-IDEAL GAS

SELF-SIMILAR FLOW UNDER THE ACTION OF MONOCHROMATIC RADIATION BEHIND A STRONG CYLINDRICAL SHOCK WAVE IN A NON-IDEAL GAS SELF-SIMILAR FLOW UNDER THE ACTION OF MONOCHROMATIC RADIATION BEHIND A STRONG CYLINDRICAL SHOCK WAVE IN A NON-IDEAL GAS *J. P. Vishwakarma and Vijay Kumar Pandey Deartment of Mathematics & Statistics,

More information

A SIMPLE PLASTICITY MODEL FOR PREDICTING TRANSVERSE COMPOSITE RESPONSE AND FAILURE

A SIMPLE PLASTICITY MODEL FOR PREDICTING TRANSVERSE COMPOSITE RESPONSE AND FAILURE THE 19 TH INTERNATIONAL CONFERENCE ON COMPOSITE MATERIALS A SIMPLE PLASTICITY MODEL FOR PREDICTING TRANSVERSE COMPOSITE RESPONSE AND FAILURE K.W. Gan*, M.R. Wisnom, S.R. Hallett, G. Allegri Advanced Comosites

More information

Paper C Exact Volume Balance Versus Exact Mass Balance in Compositional Reservoir Simulation

Paper C Exact Volume Balance Versus Exact Mass Balance in Compositional Reservoir Simulation Paer C Exact Volume Balance Versus Exact Mass Balance in Comositional Reservoir Simulation Submitted to Comutational Geosciences, December 2005. Exact Volume Balance Versus Exact Mass Balance in Comositional

More information

Meshless Methods for Scientific Computing Final Project

Meshless Methods for Scientific Computing Final Project Meshless Methods for Scientific Comuting Final Project D0051008 洪啟耀 Introduction Floating island becomes an imortant study in recent years, because the lands we can use are limit, so eole start thinking

More information

Statics and dynamics: some elementary concepts

Statics and dynamics: some elementary concepts 1 Statics and dynamics: some elementary concets Dynamics is the study of the movement through time of variables such as heartbeat, temerature, secies oulation, voltage, roduction, emloyment, rices and

More information

Mixture Homogeneous Mixtures (air, sea water ) same composition, no chemical bond components are NOT distinguishable

Mixture Homogeneous Mixtures (air, sea water ) same composition, no chemical bond components are NOT distinguishable BASIC CONCEPTAND DEFINITIONS1 2 THERMODYNAMICS CHAPTER 2 Thermodynamic Concets Lecturer Axel GRONIEWSKY, PhD 11 th of February2019 Thermodynamics study of energy and its transformation describes macroscoic

More information

FINITE TIME THERMODYNAMIC MODELING AND ANALYSIS FOR AN IRREVERSIBLE ATKINSON CYCLE. By Yanlin GE, Lingen CHEN, and Fengrui SUN

FINITE TIME THERMODYNAMIC MODELING AND ANALYSIS FOR AN IRREVERSIBLE ATKINSON CYCLE. By Yanlin GE, Lingen CHEN, and Fengrui SUN FINIE IME HERMODYNAMIC MODELING AND ANALYSIS FOR AN IRREVERSIBLE AKINSON CYCLE By Yanlin GE, Lingen CHEN, and Fengrui SUN Performance of an air-standard Atkinson cycle is analyzed by using finite-time

More information

16. CHARACTERISTICS OF SHOCK-WAVE UNDER LORENTZ FORCE AND ENERGY EXCHANGE

16. CHARACTERISTICS OF SHOCK-WAVE UNDER LORENTZ FORCE AND ENERGY EXCHANGE 16. CHARACTERISTICS OF SHOCK-WAVE UNDER LORENTZ FORCE AND ENERGY EXCHANGE H. Yamasaki, M. Abe and Y. Okuno Graduate School at Nagatsuta, Tokyo Institute of Technology 459, Nagatsuta, Midori-ku, Yokohama,

More information

The extreme case of the anisothermal calorimeter when there is no heat exchange is the adiabatic calorimeter.

The extreme case of the anisothermal calorimeter when there is no heat exchange is the adiabatic calorimeter. .4. Determination of the enthaly of solution of anhydrous and hydrous sodium acetate by anisothermal calorimeter, and the enthaly of melting of ice by isothermal heat flow calorimeter Theoretical background

More information

STATES OF MATTER UNIT 5

STATES OF MATTER UNIT 5 32 32 CHEMISTRY UNIT 5 After studying this unit you will be able to exlain the existence of different states of matter in terms of balance between intermolecular forces and thermal energy of articles;

More information

An Improved Calibration Method for a Chopped Pyrgeometer

An Improved Calibration Method for a Chopped Pyrgeometer 96 JOURNAL OF ATMOSPHERIC AND OCEANIC TECHNOLOGY VOLUME 17 An Imroved Calibration Method for a Choed Pyrgeometer FRIEDRICH FERGG OtoLab, Ingenieurbüro, Munich, Germany PETER WENDLING Deutsches Forschungszentrum

More information

1 Entropy 1. 3 Extensivity 4. 5 Convexity 5

1 Entropy 1. 3 Extensivity 4. 5 Convexity 5 Contents CONEX FUNCIONS AND HERMODYNAMIC POENIALS 1 Entroy 1 2 Energy Reresentation 2 3 Etensivity 4 4 Fundamental Equations 4 5 Conveity 5 6 Legendre transforms 6 7 Reservoirs and Legendre transforms

More information

COMPENDIUM OF EQUATIONS Unified Engineering Thermodynamics

COMPENDIUM OF EQUATIONS Unified Engineering Thermodynamics COMPENDIUM OF EQUAIONS Unified Engineering hermodynamics Note: It is with some reseration that I suly this comendium of equations. One of the common itfalls for engineering students is that they sole roblems

More information

I have not proofread these notes; so please watch out for typos, anything misleading or just plain wrong.

I have not proofread these notes; so please watch out for typos, anything misleading or just plain wrong. hermodynamics I have not roofread these notes; so lease watch out for tyos, anything misleading or just lain wrong. Please read ages 227 246 in Chater 8 of Kittel and Kroemer and ay attention to the first

More information

Unit code: H/ QCF level: 5 Credit value: 15 OUTCOME 1 - THERMODYNAMIC SYSTEMS TUTORIAL 2

Unit code: H/ QCF level: 5 Credit value: 15 OUTCOME 1 - THERMODYNAMIC SYSTEMS TUTORIAL 2 Unit 43: Plant and Process Princiles Unit code: H/60 44 QCF level: 5 Credit value: 5 OUCOME - HERMODYNAMIC SYSEMS UORIAL Understand thermodynamic systems as alied to lant engineering rocesses hermodynamic

More information

FE FORMULATIONS FOR PLASTICITY

FE FORMULATIONS FOR PLASTICITY G These slides are designed based on the book: Finite Elements in Plasticity Theory and Practice, D.R.J. Owen and E. Hinton, 1970, Pineridge Press Ltd., Swansea, UK. 1 Course Content: A INTRODUCTION AND

More information

SELF-SIMILAR FLOW OF A MIXTURE OF A NON-IDEAL GAS AND SMALL SOLID PARTICLES WITH INCREASING ENERGY BEHIND A SHOCK WAVE UNDER A GRAVITATIONAL FIELD

SELF-SIMILAR FLOW OF A MIXTURE OF A NON-IDEAL GAS AND SMALL SOLID PARTICLES WITH INCREASING ENERGY BEHIND A SHOCK WAVE UNDER A GRAVITATIONAL FIELD SELF-SIMILAR FLOW OF A MIXTURE OF A NON-IDEAL GAS AND SMALL SOLID PARTICLES WITH INCREASING ENERGY BEHIND A SHOCK WAVE UNDER A GRAVITATIONAL FIELD Vishwakarma J.P. and Prerana Pathak 1 Deartment of Mathematics

More information

4. A Brief Review of Thermodynamics, Part 2

4. A Brief Review of Thermodynamics, Part 2 ATMOSPHERE OCEAN INTERACTIONS :: LECTURE NOTES 4. A Brief Review of Thermodynamics, Part 2 J. S. Wright jswright@tsinghua.edu.cn 4.1 OVERVIEW This chater continues our review of the key thermodynamics

More information

Efficiencies. Damian Vogt Course MJ2429. Nomenclature. Symbol Denotation Unit c Flow speed m/s c p. pressure c v. Specific heat at constant J/kgK

Efficiencies. Damian Vogt Course MJ2429. Nomenclature. Symbol Denotation Unit c Flow speed m/s c p. pressure c v. Specific heat at constant J/kgK Turbomachinery Lecture Notes 1 7-9-1 Efficiencies Damian Vogt Course MJ49 Nomenclature Subscrits Symbol Denotation Unit c Flow seed m/s c Secific heat at constant J/kgK ressure c v Secific heat at constant

More information

Speed of sound measurements in liquid Methane at cryogenic temperature and for pressure up to 10 MPa

Speed of sound measurements in liquid Methane at cryogenic temperature and for pressure up to 10 MPa LNGII - raining Day Delft, August 07 Seed of sound measurements in liquid Methane at cryogenic temerature and for ressure u to 0 MPa Simona Lago*, P. Alberto Giuliano Albo INRiM Istituto Nazionale di Ricerca

More information

MODELING THE RELIABILITY OF C4ISR SYSTEMS HARDWARE/SOFTWARE COMPONENTS USING AN IMPROVED MARKOV MODEL

MODELING THE RELIABILITY OF C4ISR SYSTEMS HARDWARE/SOFTWARE COMPONENTS USING AN IMPROVED MARKOV MODEL Technical Sciences and Alied Mathematics MODELING THE RELIABILITY OF CISR SYSTEMS HARDWARE/SOFTWARE COMPONENTS USING AN IMPROVED MARKOV MODEL Cezar VASILESCU Regional Deartment of Defense Resources Management

More information

MODELING OF CONSTANT VOLUME COMBUSTION OF PROPELLANTS FOR ARTILLERY WEAPONS

MODELING OF CONSTANT VOLUME COMBUSTION OF PROPELLANTS FOR ARTILLERY WEAPONS MODELING OF CONSTANT VOLUME COMBUSTION OF PROPELLANTS FOR ARTILLERY WEAPONS Lt.col. lect. dr.ing. Daniel ANTONIE, Col.(r). rof.as. dr.ing. Sorin GHEORGHIAN, Col.(r). C.S.II dr.ing. Nicolae MĂRUNȚELU MILITARY

More information

Towards understanding the Lorenz curve using the Uniform distribution. Chris J. Stephens. Newcastle City Council, Newcastle upon Tyne, UK

Towards understanding the Lorenz curve using the Uniform distribution. Chris J. Stephens. Newcastle City Council, Newcastle upon Tyne, UK Towards understanding the Lorenz curve using the Uniform distribution Chris J. Stehens Newcastle City Council, Newcastle uon Tyne, UK (For the Gini-Lorenz Conference, University of Siena, Italy, May 2005)

More information

High speed wind tunnels 2.0 Definition of high speed. 2.1 Types of high speed wind tunnels

High speed wind tunnels 2.0 Definition of high speed. 2.1 Types of high speed wind tunnels Module Lectures 6 to 1 High Seed Wind Tunnels Keywords: Blow down wind tunnels, Indraft wind tunnels, suersonic wind tunnels, c-d nozzles, second throat diffuser, shocks, condensation in wind tunnels,

More information

Introduction to Landau s Fermi Liquid Theory

Introduction to Landau s Fermi Liquid Theory Introduction to Landau s Fermi Liquid Theory Erkki Thuneberg Deartment of hysical sciences University of Oulu 29 1. Introduction The rincial roblem of hysics is to determine how bodies behave when they

More information

AT 25 C! CH10090 Thermodynamics (part 2) Enthalpy changes during reactions. Let s remember what we did in CH10089

AT 25 C! CH10090 Thermodynamics (part 2) Enthalpy changes during reactions. Let s remember what we did in CH10089 CH10090 hermodynamics (art ) Let s remember what we did in CH10089 Enthaly changes during reactions o o o H98 ( reaction) = νi Hf, 98( roducts) νi Hf, 98( reactants) ν i reresents the stoichiometric coefficient.

More information

ONE. The Earth-atmosphere system CHAPTER

ONE. The Earth-atmosphere system CHAPTER CHAPTER ONE The Earth-atmoshere system 1.1 INTRODUCTION The Earth s atmoshere is the gaseous enveloe surrounding the lanet. Like other lanetary atmosheres, it figures centrally in transfers of energy between

More information

Chapter 6. Thermodynamics and the Equations of Motion

Chapter 6. Thermodynamics and the Equations of Motion Chater 6 hermodynamics and the Equations of Motion 6.1 he first law of thermodynamics for a fluid and the equation of state. We noted in chater 4 that the full formulation of the equations of motion required

More information

Lecture 13. Heat Engines. Thermodynamic processes and entropy Thermodynamic cycles Extracting work from heat

Lecture 13. Heat Engines. Thermodynamic processes and entropy Thermodynamic cycles Extracting work from heat Lecture 3 Heat Engines hermodynamic rocesses and entroy hermodynamic cycles Extracting work from heat - How do we define engine efficiency? - Carnot cycle: the best ossible efficiency Reading for this

More information

Maximum Power Output of Quantum Heat Engine. with Energy Bath

Maximum Power Output of Quantum Heat Engine. with Energy Bath Maximum Power Outut of Quantum Heat Engine with Energy Bath Shengnan Liu, Congjie Ou, College of Information Science and Engineering, Huaqiao University, Xiamen 360, China; 30008003@hqu.edu.cn Corresondence:

More information

PROCESSING OF LOW-VISCOSITY CBT THERMOPLASTIC COMPOSITES: HEAT TRANSFER ANALYSIS

PROCESSING OF LOW-VISCOSITY CBT THERMOPLASTIC COMPOSITES: HEAT TRANSFER ANALYSIS PROCESSING OF LOW-VISCOSITY CBT THERMOPLASTIC COMPOSITES: HEAT TRANSFER ANALYSIS Dr. Adrian Murtagh, Siora Coll and Dr. Conchúr Ó Brádaigh Comosites Research Unit Det. of Mechanical & Biomedical Engineering,

More information

Pretest (Optional) Use as an additional pacing tool to guide instruction. August 21

Pretest (Optional) Use as an additional pacing tool to guide instruction. August 21 Trimester 1 Pretest (Otional) Use as an additional acing tool to guide instruction. August 21 Beyond the Basic Facts In Trimester 1, Grade 8 focus on multilication. Daily Unit 1: Rational vs. Irrational

More information

On the relationship between sound intensity and wave impedance

On the relationship between sound intensity and wave impedance Buenos Aires 5 to 9 Setember, 16 Acoustics for the 1 st Century PROCEEDINGS of the nd International Congress on Acoustics Sound Intensity and Inverse Methods in Acoustics: Paer ICA16-198 On the relationshi

More information

Lecture 13 Heat Engines

Lecture 13 Heat Engines Lecture 3 Heat Engines hermodynamic rocesses and entroy hermodynamic cycles Extracting work from heat - How do we define engine efficiency? - Carnot cycle: the best ossible efficiency Reading for this

More information

Kinetics of Protein Adsorption and Desorption on Surfaces with Grafted Polymers

Kinetics of Protein Adsorption and Desorption on Surfaces with Grafted Polymers 1516 Biohysical Journal Volume 89 Setember 2005 1516 1533 Kinetics of Protein Adsortion and Desortion on Surfaces with Grafted Polymers Fang Fang,* Javier Satulovsky, y and Igal Szleifer* *Deartment of

More information

Numerical and experimental investigation on shot-peening induced deformation. Application to sheet metal forming.

Numerical and experimental investigation on shot-peening induced deformation. Application to sheet metal forming. Coyright JCPDS-International Centre for Diffraction Data 29 ISSN 197-2 511 Numerical and exerimental investigation on shot-eening induced deformation. Alication to sheet metal forming. Florent Cochennec

More information

A short note on Reitlinger thermodynamic cycles

A short note on Reitlinger thermodynamic cycles short note on Reitlinger thermodynamic cycles melia arolina Saravigna eartment of lied Science and echnology, Politecnico di orino, orino, Italy bstract: It is well known that arnot cycle is the thermodynamic

More information

INTRODUCING THE SHEAR-CAP MATERIAL CRITERION TO AN ICE RUBBLE LOAD MODEL

INTRODUCING THE SHEAR-CAP MATERIAL CRITERION TO AN ICE RUBBLE LOAD MODEL Symosium on Ice (26) INTRODUCING THE SHEAR-CAP MATERIAL CRITERION TO AN ICE RUBBLE LOAD MODEL Mohamed O. ElSeify and Thomas G. Brown University of Calgary, Calgary, Canada ABSTRACT Current ice rubble load

More information

Chemistry 420/523 Chemical Thermodynamics (Spring ) Examination 1

Chemistry 420/523 Chemical Thermodynamics (Spring ) Examination 1 Chemistry 420/523 Chemical hermodynamics (Sring 2001-02) Examination 1 1 Boyle temerature is defined as the temerature at which the comression factor Z m /(R ) of a gas is exactly equal to 1 For a gas

More information

Modeling Volume Changes in Porous Electrodes

Modeling Volume Changes in Porous Electrodes Journal of The Electrochemical Society, 53 A79-A86 2006 003-465/2005/53/A79/8/$20.00 The Electrochemical Society, Inc. Modeling olume Changes in Porous Electrodes Parthasarathy M. Gomadam*,a,z John W.

More information

Chapter 9 Practical cycles

Chapter 9 Practical cycles Prof.. undararajan Chater 9 Practical cycles 9. Introduction In Chaters 7 and 8, it was shown that a reversible engine based on the Carnot cycle (two reversible isothermal heat transfers and two reversible

More information

Analysis of Pressure Transient Response for an Injector under Hydraulic Stimulation at the Salak Geothermal Field, Indonesia

Analysis of Pressure Transient Response for an Injector under Hydraulic Stimulation at the Salak Geothermal Field, Indonesia roceedings World Geothermal Congress 00 Bali, Indonesia, 5-9 Aril 00 Analysis of ressure Transient Resonse for an Injector under Hydraulic Stimulation at the Salak Geothermal Field, Indonesia Jorge A.

More information

Numerical simulation of bird strike in aircraft leading edge structure using a new dynamic failure model

Numerical simulation of bird strike in aircraft leading edge structure using a new dynamic failure model Numerical simulation of bird strike in aircraft leading edge structure using a new dynamic failure model Q. Sun, Y.J. Liu, R.H, Jin School of Aeronautics, Northwestern Polytechnical University, Xi an 710072,

More information

Domain Dynamics in a Ferroelastic Epilayer on a Paraelastic Substrate

Domain Dynamics in a Ferroelastic Epilayer on a Paraelastic Substrate Y. F. Gao Z. Suo Mechanical and Aerosace Engineering Deartment and Princeton Materials Institute, Princeton University, Princeton, NJ 08544 Domain Dynamics in a Ferroelastic Eilayer on a Paraelastic Substrate

More information

Ideal Gas Law. September 2, 2014

Ideal Gas Law. September 2, 2014 Ideal Gas Law Setember 2, 2014 Thermodynamics deals with internal transformations of the energy of a system and exchanges of energy between that system and its environment. A thermodynamic system refers

More information

Author(s) Tohei, T; Kuwabara, A; Yamamoto, T; Citation PHYSICAL REVIEW LETTERS (2005), 94(

Author(s) Tohei, T; Kuwabara, A; Yamamoto, T; Citation PHYSICAL REVIEW LETTERS (2005), 94( Title General rule for dislacive comounds revisited by first hase rinci t Author(s) Tohei, T; Kuwabara, A; Yamamoto, T; Citation PHYSICAL REVIEW LETTERS (2005), 94( Issue Date 2005-01-28 URL htt://hdl.handle.net/2433/39924

More information

Where: Where: f Wave s frequency (Hz) c Speed of light ( ms -1 ) Wavelength (m)

Where: Where: f Wave s frequency (Hz) c Speed of light ( ms -1 ) Wavelength (m) in a direction to both of the fields as shown in Figure 1. In wave model, the electromagnetic radiation is commonly associated with wavelength and frequency, exressed mathematically as: c f...(1) f Wave

More information

The International Association for the Properties of Water and Steam

The International Association for the Properties of Water and Steam IAPWS SR5-05(2016) he International Association for the Proerties of Water and Steam Moscow, Russia June 2014 Revised Sulementary Release on Backward Equations for Secific Volume as a Function of Pressure

More information

A Numerical Method for Critical Buckling Load for a Beam Supported on Elastic Foundation

A Numerical Method for Critical Buckling Load for a Beam Supported on Elastic Foundation A Numerical Method for Critical Buckling Load for a Beam Suorted on Elastic Foundation Guo-ing Xia Institute of Bridge Engineering, Dalian University of Technology, Dalian, Liaoning Province, P. R. China

More information

PHYSICAL REVIEW LETTERS

PHYSICAL REVIEW LETTERS PHYSICAL REVIEW LETTERS VOLUME 81 20 JULY 1998 NUMBER 3 Searated-Path Ramsey Atom Interferometer P. D. Featonby, G. S. Summy, C. L. Webb, R. M. Godun, M. K. Oberthaler, A. C. Wilson, C. J. Foot, and K.

More information

Deriving Indicator Direct and Cross Variograms from a Normal Scores Variogram Model (bigaus-full) David F. Machuca Mory and Clayton V.

Deriving Indicator Direct and Cross Variograms from a Normal Scores Variogram Model (bigaus-full) David F. Machuca Mory and Clayton V. Deriving ndicator Direct and Cross Variograms from a Normal Scores Variogram Model (bigaus-full) David F. Machuca Mory and Clayton V. Deutsch Centre for Comutational Geostatistics Deartment of Civil &

More information

Characteristics of Beam-Based Flexure Modules

Characteristics of Beam-Based Flexure Modules Shorya Awtar e-mail: shorya@mit.edu Alexander H. Slocum e-mail: slocum@mit.edu Precision Engineering Research Grou, Massachusetts Institute of Technology, Cambridge, MA 039 Edi Sevincer Omega Advanced

More information

Finite Element Analysis of V-Bending of Polypropylene Using Hydrostatic-Pressure-Dependent Plastic Constitutive Equation*

Finite Element Analysis of V-Bending of Polypropylene Using Hydrostatic-Pressure-Dependent Plastic Constitutive Equation* Materials Transactions, Vol. 48, No. 1 (7). 6 to 664 #7 The Jaan Society for Technology of Plasticity Finite Element Analysis of V-Bending of Polyroylene Using Hydrostatic-Pressure-Deendent Plastic onstitutive

More information

Explosion Protection of Buildings

Explosion Protection of Buildings 1 Exlosion Protection of Buildings Author: Miroslav Mynarz 2 Exlosion Protection of Buildings Exlosion of a Condensed Exlosive and Calculation of Blast Wave Parameters Theory of exlosion of condensed exlosive

More information

Research of power plant parameter based on the Principal Component Analysis method

Research of power plant parameter based on the Principal Component Analysis method Research of ower lant arameter based on the Princial Comonent Analysis method Yang Yang *a, Di Zhang b a b School of Engineering, Bohai University, Liaoning Jinzhou, 3; Liaoning Datang international Jinzhou

More information

Physics 2A (Fall 2012) Chapters 11:Using Energy and 12: Thermal Properties of Matter

Physics 2A (Fall 2012) Chapters 11:Using Energy and 12: Thermal Properties of Matter Physics 2A (Fall 2012) Chaters 11:Using Energy and 12: Thermal Proerties of Matter "Kee in mind that neither success nor failure is ever final." Roger Ward Babson Our greatest glory is not in never failing,

More information

Minimum Fluidization Velocities of Binary- Solid Mixtures: Model Comparison

Minimum Fluidization Velocities of Binary- Solid Mixtures: Model Comparison Vol:4, No:3, 00 Minimum Fluidization Velocities of Binary- Solid Mixtures: Model Comarison Mohammad Asif International Science Index, Chemical and Molecular Engineering Vol:4, No:3, 00 waset.org/publication/5950

More information

Preliminary Uncertainty Estimation of the Pressure Distortion Coefficient of a Pressure. Balance by FEM Calculations

Preliminary Uncertainty Estimation of the Pressure Distortion Coefficient of a Pressure. Balance by FEM Calculations Preliminary Uncertainty Estimation of the Pressure Distortion Coefficient of a Pressure Balance by FEM Calculations G. Molinar*, M. Bergoglio*, G. Mosso*,G. Buonanno**, M. Dell Isola** * Istituto di Metrologia

More information

Lower bound solutions for bearing capacity of jointed rock

Lower bound solutions for bearing capacity of jointed rock Comuters and Geotechnics 31 (2004) 23 36 www.elsevier.com/locate/comgeo Lower bound solutions for bearing caacity of jointed rock D.J. Sutcliffe a, H.S. Yu b, *, S.W. Sloan c a Deartment of Civil, Surveying

More information

Chapter-6: Entropy. 1 Clausius Inequality. 2 Entropy - A Property

Chapter-6: Entropy. 1 Clausius Inequality. 2 Entropy - A Property hater-6: Entroy When the first law of thermodynamics was stated, the existence of roerty, the internal energy, was found. imilarly, econd law also leads to definition of another roerty, known as entroy.

More information

Flexible Pipes in Trenches with Stiff Clay Walls

Flexible Pipes in Trenches with Stiff Clay Walls Flexible Pies in Trenches with Stiff Clay Walls D. A. Cameron University of South Australia, South Australia, Australia J. P. Carter University of Sydney, New South Wales, Australia Keywords: flexible

More information

Maximum Entropy and the Stress Distribution in Soft Disk Packings Above Jamming

Maximum Entropy and the Stress Distribution in Soft Disk Packings Above Jamming Maximum Entroy and the Stress Distribution in Soft Disk Packings Above Jamming Yegang Wu and S. Teitel Deartment of Physics and Astronomy, University of ochester, ochester, New York 467, USA (Dated: August

More information

Modelling heat transfer and fluid flow inside a pressure cooker

Modelling heat transfer and fluid flow inside a pressure cooker 17 th Euroean Symosium on Comuter Aided Process Engineering ESCAPE17 V. Plesu and P.S. Agachi (Editors) 2007 Elsevier B.V. All rights reserved. 1 Modelling heat transfer and fluid flow inside a ressure

More information

The temperature dependence of the isothermal bulk modulus at 1 bar pressure

The temperature dependence of the isothermal bulk modulus at 1 bar pressure he temerature deendence of the isothermal bulk modulus at bar ressure J. Garai a) Det. of Earth Sciences, Florida International University, University Park, PC 344, Miami, FL 3399, USA A. Laugier IdPCES

More information

Characterization of Material Parameters

Characterization of Material Parameters Proceedings of the World Congress on Engineering 29 Vol II WCE 29, July 1-3, 29, London, U.K. Characterization of Material Parameters S. M. Humayun Kabir, Tae-In Yeo, Sang-Ho Kim Abstract The resent work

More information

The thermal wind 1. v g

The thermal wind 1. v g The thermal win The thermal win Introuction The geostrohic win is etermine by the graient of the isobars (on a horizontal surface) or isohyses (on a ressure surface). On a ressure surface the graient of

More information

df da df = force on one side of da due to pressure

df da df = force on one side of da due to pressure I. Review of Fundamental Fluid Mechanics and Thermodynamics 1. 1 Some fundamental aerodynamic variables htt://en.wikiedia.org/wiki/hurricane_ivan_(2004) 1) Pressure: the normal force er unit area exerted

More information

A Simple And Efficient FEM-Implementation Of The Modified Mohr-Coulomb Criterion Clausen, Johan Christian; Damkilde, Lars

A Simple And Efficient FEM-Implementation Of The Modified Mohr-Coulomb Criterion Clausen, Johan Christian; Damkilde, Lars Aalborg Universitet A Simle And Efficient FEM-Imlementation Of The Modified Mohr-Coulomb Criterion Clausen, Johan Christian; Damkilde, Lars Published in: Proceedings of the 9th Nordic Seminar on Comutational

More information

Surface relaxation and surface energy of face centered Cubic metals

Surface relaxation and surface energy of face centered Cubic metals JASEM ISSN 1119-8362 All rights reserved Full-text Available Online at www.bioline.org.br/ja J. Al. Sci. Environ. Mgt. March 2006 Vol. 10 (1) 37. - 42 Surface relaxation and surface energy of face centered

More information

A compression line for soils with evolving particle and pore size distributions due to particle crushing

A compression line for soils with evolving particle and pore size distributions due to particle crushing Russell, A. R. (2011) Géotechnique Letters 1, 5 9, htt://dx.doi.org/10.1680/geolett.10.00003 A comression line for soils with evolving article and ore size distributions due to article crushing A. R. RUSSELL*

More information

Supplementary Material: Crumpling Damaged Graphene

Supplementary Material: Crumpling Damaged Graphene Sulementary Material: Crumling Damaged Grahene I.Giordanelli 1,*, M. Mendoza 1, J. S. Andrade, Jr. 1,, M. A. F. Gomes 3, and H. J. Herrmann 1, 1 ETH Zürich, Comutational Physics for Engineering Materials,

More information

PERFORMANCE BASED DESIGN SYSTEM FOR CONCRETE MIXTURE WITH MULTI-OPTIMIZING GENETIC ALGORITHM

PERFORMANCE BASED DESIGN SYSTEM FOR CONCRETE MIXTURE WITH MULTI-OPTIMIZING GENETIC ALGORITHM PERFORMANCE BASED DESIGN SYSTEM FOR CONCRETE MIXTURE WITH MULTI-OPTIMIZING GENETIC ALGORITHM Takafumi Noguchi 1, Iei Maruyama 1 and Manabu Kanematsu 1 1 Deartment of Architecture, University of Tokyo,

More information

Adiabatic Shear Bands in Simple and Dipolar Plastic Materials

Adiabatic Shear Bands in Simple and Dipolar Plastic Materials Adiabatic Shear Bands in Simle and Diolar Plastic Materials T W \-1RIGHT us Army Ballistic Research Laboratory Aberdeen Proving Ground, MD 215 R C BATRA University of Missouri-Rolla Rolla, Missouri 6541

More information

Lecture 8, the outline

Lecture 8, the outline Lecture, the outline loose end: Debye theory of solids more remarks on the first order hase transition. Bose Einstein condensation as a first order hase transition 4He as Bose Einstein liquid Lecturer:

More information

Chapter 6: Sound Wave Equation

Chapter 6: Sound Wave Equation Lecture notes on OPAC0- ntroduction to Acoustics Dr. Eser OLĞAR, 08 Chater 6: Sound Wave Equation. Sound Waves in a medium the wave equation Just like the eriodic motion of the simle harmonic oscillator,

More information

REAL GASES. (B) pv. (D) pv. 3. The compressibility factor of a gas is less than unity at STP. Therefore, molar volume (V m.

REAL GASES. (B) pv. (D) pv. 3. The compressibility factor of a gas is less than unity at STP. Therefore, molar volume (V m. SINGLE ORRET ANSWER REAL GASES 1. A real gas is suosed to obey the gas equation ( b) = at STP. If one mole of a gas occuies 5dm 3 volume at STP, then its comressibility factor is (b=.586 L mol 1F) (A)

More information

AE301 Aerodynamics I UNIT A: Fundamental Concepts

AE301 Aerodynamics I UNIT A: Fundamental Concepts AE301 Aerodynamics I UNIT A: Fundamental Concets ROAD MAP... A-1: Engineering Fundamentals Reiew A-: Standard Atmoshere A-3: Goerning Equations of Aerodynamics A-4: Airseed Measurements A-5: Aerodynamic

More information

1 Properties of Spherical Harmonics

1 Properties of Spherical Harmonics Proerties of Sherical Harmonics. Reetition In the lecture the sherical harmonics Y m were introduced as the eigenfunctions of angular momentum oerators lˆz and lˆ2 in sherical coordinates. We found that

More information