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Static of fluids A fluid has constant volume and the shape of its container Law n 1: a fluid at rest cannot produce a force tangent to the surface (no shear force), the normal force does not depend on the orientation of the surface Pressure F F N p= , [ 2 ≡ P ascal = P a] A m p → mean pressure; F → normal force acting on the surface A. hydraulic A press Law n. 2 (Pascal): the pressure in a fluid (neglecting the gravitational force) is the same everywhere in the fluid. m Kg ρ= , [ 3] Density F1 F2 V m ≡ A1 A2 ρ → (local) density of the body; m mass of the body contained in a section of volume V of the body. F0 Stevino’s law Fg = ρAhg p = p0 + ρgh F p → pressure acting at dept h; p0 → pressure acting on the free surface of the liquid; ρ → density of the liquid. Communicating vessels p A ≡ pB → h A ≡ h B if p0 is the same in both the vassels P0 Manometer h Pa Pa F A ≡ FB p A ≡ pB Relative (gauge) pressure ∆p = pa − p0 = ρg(ha − h0 ) = ρgh 1 atm = 760 mm Hg = 1.0133 × 105 Pa Archimedes’ law F2 − F1 = (p2 − p1 )A = Aρf g(h2 − h1 ) = V ρf g = mf g FA = mf g Fg = mc g p1 p2 FA = ρf · g · Vc FA → Archimedes’ force (acting upward); ρf → density of the fluid; Vc → volume of the body immersed in the fluid ρf > ρc Archimedes’ force wins on the gravity force ρf = ρc equilibriumù ρf < ρc gravity force wins on Archimedes’ force Vi ρc = Vc ρf ρc = density of the body ( Vmc ); Vi volume of the immersed part of the body; Vc total volume of the body Dynamics of ideal fluids Continuity equation ρf · A · v = cost = mass flow rate ρf = fluid density; A = area of the conductor section in which the fluid flows; v fluid velocity through the section Q = Vt volume flow rate For a incompressible fluid (ρ = cost) we have: A · v = m3 Q = cost , [ s ] Q = Vt = Ad d = A · v = volume flow rate v Bernoulli’s equation (stationary and incompressible fluids) p + ρgh + 12 ρv 2 = cost p pressure acting on the considered section, ρ fuid density; h mean level of the section w.r.t. a reference; v fluid velocity through the section Dynamics of real fluids real fluid moves laminar flow (es: blood in small vassells) Fη = ηSvm R = η(2πRL)v R = 2πηLvm Poiseulle’s law (flow on a cylindric conductor at laminar regime) πR4 (p1 − p2 ) Q= 8η L R = radius of the pipeline; L = length of the pipeline; p1 − p2 = difference of pressure at the ends of the pipeline; ·s η[ N m2 ] = friction coefficient due to the fluid viscosity. Poiseuille’s law: the flow of fluid through a section of the pipeline is proportional to the difference of pressure in the pipeline and to the fourth power of the pipeline radius vm (p1 − p2 )R2 = 4ηL Surface tension On the surfaces of separation between liquid and other materials act forces of molecular attraction In small vessels (capillary < 1 mm) the surface forces raise or lower the liquid according to the law: 2τ cosα h= R·ρ·g Where: τ [N/m] = is the surface force: force per unit of length tangent to the surface. R vessel radius; ρ fluid density; α angle between the surface of the liquid and the walls of the vessel; h is the level ho de meniscus ( > 0 concave meniscus, < 0 convex meniscus) of the fluid. α α Heat and temperature Thermometric scales Triple point of water 273.16 K (0.01°C) Boiling point of water 100.00°C 373.15 K 212.00°F Freezing point of water 0.00°C 273.15 K 32.00°F Absolute zero -273.15°C 0K -459.67°F Thermal expansion in solids and fluids ∆l = li · λ · ∆T ∆A = Ai · σ · ∆T ∆V = Vi · γ · ∆T ∆l, ∆A, ∆V variation of length, area or volume; li , Ai , Vi initial values, ∆T variation of temperature; λ, σ, γ[o C −1 ] coefficients of expansion. Heat absorbed or lost by a body Q = m · c · ∆T = C · ∆T dove C = m · c Q heat ABSORBED (Q > 0) or LOST (Q < 0) by a body (in which there are not phase transitions); ∆T variation of temperature; m mass of the body; c [cal / Kg o C] specific heat; C [cal / o C] heat capacity of the body In purely thermal transformations the heat is conserved Heat (latent) of transition A = Lm, where L is the specific latent heat cH2 0 = 1.00 gcal 0C Thermal equilibrium Heat is a form of energy 1Cal = 4.186J Heat is a form of energy, thus it is expressed in Joule in the IS. Another unit of common use is the calorie (cal) As we will see, in general energy + heat is conserved in an isolated system (first principle of thermodynamics) Heat transfer mechanisms Conduction: The exchanged heat Q in a time t through a section of area A of a body of length l with thermal conductivity k [cal/ m s o C] whose ends are at temperatures T1 e T2 is: T2 − T1 Q=k·A ·t l Convection: Irradiation: Power P [Watt] irradiated or absorbed (Tc > Ta or Ta > Tc ) by a surface of area A with emissivity � ∈ [0, 1] at temperature Tc in an environment at temperature Ta is: σ = 5.67 · 10−8 W / m2 K4 costante di Stefan-Boltzmann. P = � · σ · A · (Tc4 − Ta4 ) Ideal gas Dimensionless, massless moleculas interacting only through perfect elastic collisions VT = V0 (1 + γT ) with γ = 1 273.15o C Ideal gas law p · V = nRT p e V pressure and volume of the ideal gas; T temperature in KELVIN; R = 8.3144 [J / K mole] Universal constant of gasses; n number of moles. A mole of a substance contains NA = 6.02·1023 molecules; NA Avogadro number. k= R Na = 1.38 · 10−23 J/ K is the Boltzmann constant. Ideal gas transformations p · V = nRT p e V pressione e volume del gas;pressure T temperatura in KELVIN; Transformation at constant (ISOBARE): 8.3144 [J / K mole] COSTANTE UNIVERSALE DEI pR==cost GAS; n numero moli. Transformation at constant volume (ISOCORE): 23 Una mole di qualsiasi sostanza contiene NA = 6.02·10 Vmolecole; = cost N numero di Avogadro. A Transformation at constant temperature (ISOTERME): T = cost → p · V = cost Transformation without heat exchange (ADIABATIC): Q = cost Thermal bath Q = Cp ∆T : Cp = specific heat at constant pressure. Q = Cv ∆T : Cv = specific heat at constant pressure. Equipartition of energy In the motion of molecules in a gas at a given temperature, to every independent component of the motion (degree of freedom) corresponds the same kinetic energy Km 1 = kT 2 where k = NRA = 1.38 · 10−23 J / mole K is the Blotzmann constant The total kinetic energy of a molecule is Km = λ kT 2 λ = degrees of freedom: monoatomic molecules λ = 3; diatomic molecules λ = 5; pluriatomic molecules λ = 6. Thermodynamics First principle of thermodynamics The variation of internal energy of a system (∆U ) is equal to the energy exchanged with the external with the external environment (∆U = −∆EE ). ∆U = Q − W ∆U = variation of internal energy of the system; Q heat absorbed (> 0) by the system; W work done (> 0) by the system Thermodynamics ∆U = Q − W ∆U = variation of internal energy of the system; Q heat absorbed (> 0) by the system; W work done (> 0) by the system Reversible transformations Constant volume: ∆V = 0 ⇒ W = p∆V = 0 ∆U = Q − W = Q = nCv ∆T , Q > 0 ⇒ ∆U > 0 Constant pressure: ∆p = 0, W = nR∆T , Q = nCp ∆T ∆U = Q − W = ncp ∆T − nR∆T = ncv ∆T → cp − cv = R Constant temperature: ∆T = 0 → ∆U = 0 → Q = W Thermal bath Adiabatic: Q = 0 → ∆U = −W = nCv ∆T Carnot cycle Reversible transformations Rendimento del ciclo di Carnot Wciclo = Q2 − Q1 =, Q1 = Heat absorbed by the refrigerator, Q2 = Heat absorbed by the source. Q1 T2 −T1 T1 ciclo = 1 − = = 1 − η = WQ Q2 T2 T2 2 ⇒0≤η<1 Second principle of thermodynamics It is impossible to realize a cyclic machine whose only result is to transform in work all the heat absorbed by a homogeneous source (Kelvin-Planck formulation). The efficiency ηirr of a real cyclic machine (Irreversible) working among two temperatures T1 and T2 is less than the efficiency of a corresponding Carnot cycle ηirr < ηrev . Chaos in the universe tends to increase The chaotic configurations are statistically more probable Entropy is a function of state which can be defined for reversible processes by mens of the heat ∆Qrev exchanged by the system and the corresponding instantaneous temperature T: ∆Qrev ∆S = , [J/K] T Variation of entropy in a reversible cycle: ∆Srev = 0. ∆Q Otherwise: ∆QTirr < Tref For every real isolated system (adibatic): ∆S ≥ 0 Entropy is a function of state which can be defined for reversible processes by mens of the heat ∆Qrev exchanged by the system and the corresponding instantaneous temperature T: ∆Qrev ∆S = , [J/K] T The entropy describes the disorder of a system: if the macroscopic system is characterised by D possible equivalent micro-states (disorder), then S ∝ log D Second principle ⇒ the chaos in the universe increases. Third principle of thermodynamics The absolute entropy of a crystallin solid at the temperature of 0 K is zero. Real gases Phase transitions Q = m · cl In the isotherm process of phase transition a body absorbs or give a quantity Q of heat where m is the mass and cL is the latent heat. Newton’s law of cooling T (t) = Ti e−kt , k = gradient of the cooling.