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Introduction - Physical Chemistry I - Handout, Exercises of Physical Chemistry

MAin topics of this course are: States of Matter, Energies of Molecules, Thermochemistry, Entropy, Equilibrium and Spontaneity, Quantum Chemistry. This lecture includes: Introduction, Physical Chemistry, Thermodynamics, Quantum Mechanics, Statistical Mechanics, Thermodynamics and Kinetics, Macroscopic, Atoms and Molecules, Tobacco Mosaic Virus, Biological Systems

Typology: Exercises

2012/2013

Uploaded on 09/26/2013

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Download Introduction - Physical Chemistry I - Handout and more Exercises Physical Chemistry in PDF only on Docsity! 0. Introduction physical chemistry establishes and develops the principles of chemistry concepts used to explain and interpret observations on the physical and chemical properties of matter central theme: • systems • states • processes topics of physical chemistry: (1) the study of the macroscopic properties of sys- tems of many atoms or molecules (2) the study of processes which such systems can undergo (3) the study of the properties of individual atoms and molecules PChem I 1.1 (4) the study of the relationship between microscop- ic (atomic or molecular) properties and macroscopic properties main areas of physical chemistry thermodynamics (1) and (2) quantum mechanics (3) statistical mechanics (4) kinetics and transport (2) and (3) this semester: topics (1) and (2), i.e., equilibrium thermodynamics and kinetics focus on systems of many elementary building blocks, large (classical) systems N =O(NA) macroscopic viewpoint: “forget” the existence of atoms and molecules −→ physical chemistry more abstract (and more mathematical) than other chemistry courses example of a thermodynamic system: water, pure H2O, say 1 L at ambient pressure (1 atm) PChem I 1.2 further examples of thermodynamic systems: cell in a nutrient solution, mitochondrion in a cell (??) are these large systems? is thermodynamics applica- ble to these biological systems? [ATP] ∼ 10−3 mol L−1 = 10−3 M = 1 mM, size of a mi- tochondrion: diameter ∼ 0.5 µm, length ∼ 2 µm =⇒ NATP ∼ 200000; macroscopic? [H+] ∼ 10−7 M (neutral pH) =⇒ NH+ ∼ 20; macroscop- ic?? importance of fluctuations if the average ∼ N , then the variance ∼ pN =⇒ relative strength of fluctuations ∼ 1/pN (p N N = 1pN ) ATP: fluctuations ∼ 1/p200000 = 2×10−3 H+: fluctuations ∼ 1/p20 = 2×10−1 macroscopic system: sufficiently large number N of atoms, molecules, ions, . . . , such that 1/ p N ¿ 1 PChem I 1.5 Thermodynamics large systems two types of variables: intensive – extensive T , P , . . . V , m, . . . historically: empirical observations concerning rela- tions between such variables example: PV = nRT origins of thermodynamics: practical interest: heat generates motion evolved into a theory that describes transformation of states of matter in general thermodynamics is particular good in dealing with complex systems, since the exact nature of the con- stituents and microscopic processes is irrelevant two conceptual innovations of thermodynamics First Law: conservation of energy Second Law: entropy PChem I 1.6 1. The Properties of Gases Notation: (i) I use an overbar to denote molar quan- tities; the textbook uses a subscript m. Example: mo- lar volume, these notes V , textbook Vm. (ii) I use a capital P for pressure; the textbook uses p. simple system to learn the concepts and methods of thermodynamics gas: fills any container dilute gas; chemically pure macroscopic description state of pure gas: V volume of container, T temper- ature of the gas, P pressure of the gas, n amount of the gas = number of moles assume no electric or magnetic properties pressure P = F A PChem I 1.7 thermodynamic temperature scale: Θ◦C, melting point of ice: 0◦C at 1 atm; boiling point of water: 100◦C at 1 atm T K ≡ Θ◦C +273.15 thermodynamic equilibrium = thermal equilibrium, TA = TB and mechanical equilibrium, PA = PB thermodynamic equilibrium states P = f (n,V , T ) ideal gas PV = nRT SI units: V m3, P Pa, T K: R = 8.314 J K−1mol−1 PChem I 1.10 1 J = 1 N m alternative units: V L, (1 L = 1 dm3 = 10−3 m3) P atm: R = 8.206×10−2 L atm K−1mol−1 consider a system with n = const isotherm: T = const, PV = const, P ∼ 1/V , hyperbolas [Figure: Ideal gas isotherms; Atkins 9th ed., Fig. 1.4] PChem I 1.11 isobar: P = const, V ∼ T [Figure: Ideal gas isobars; Atkins 9th ed., Fig. 1.6] PChem I 1.12 T = 298.15 K, P = 1 bar =⇒ V = RT /P = 24.789 dm3mol−1 mixture of ideal gases Dalton’s law P = P1+P2+ . . . = ∑ j P j , P j = n j RT V mole fraction x j = n j n , n =∑ j n j P j = x j P for nonideal gases: P j ≡ x j P Real Gases deviations from ideal gas law: due to intermolecular forces PChem I 1.15 [Figure: Potential energy between two molecules; Atkins 9th ed., Fig. 1.13] attractive: dipole-dipole forces, H-bonds, dispersion forces repulsive: repulsion of electrons measure for deviations compression factor Z = PV RT PChem I 1.16 ideal gas (superscript ◦) V ◦ = RT P ⇒ Z ◦ ≡ 1 Z = V V ◦ [Figure: Compression factor; Atkins 9th ed., Fig. 1.14] Z > 1 ⇒V >V ◦ repulsive forces dominate Z < 1 ⇒V <V ◦ attractive forces dominate PChem I 1.17 Boyle temperature TB: B ′(TB) = 0 or B(TB) = 0 P → 0: if T = TB then Z → 1 and dZ /dP → 0 ⇒ extended range of ideal behavior [Figure: Boyle temperature; Atkins 9th ed., Fig. 1.16] Boyle temperatures for some gases: H2 109 K, CH4 510 K, C2H4 720 K, NH3 1030 K [Estrada-Torres, R.; Iglesias-Silva, G. A.; Ramos-Estrada, M. & Hall, K. R., Boyle temper- atures for pure substances, Fluid Phase Equilib., 258, 148–154 (2007), http://dx.doi.org/10.1016/j.fluid.2007.06.004] PChem I 1.20 real gas isotherms: example CO2 [Figure: CO2 isotherms; Atkins 9th ed., Fig. 1.15] phase transition: condensation, gas −→ liquid critical point: critical temperature = maximum tem- perature at which a gas can be liquefied PChem I 1.21 phase diagram critical temperature Tc, critical pressure Pc, critical molar volume V c: critical constants as the critical point is approached along the vapor pressure curve: ρ(l )−ρ(g ) → 0 or V (g )−V (l ) → 0 PChem I 1.22 continuity of states: the substance changes from liquid-like to gas-like in the supercritical region with- out ever changing phases virial equation of state good for quantitative work, B(T ), C (T ), . . . are tabulated for gases, but it does not provide understanding of the above phenomena of real gases find a “general” model; best known and most widely used: van der Waals gas repulsive interactions: hard spheres ⇒ excluded vol- ume, V →V −nb b is a material constant, equal to the volume of 1 mol of densely packed gas particles P (V −nb) = nRT or P = nRT V −nb PChem I 1.25 attractive forces: diminish pressure; pressure is the result of collisions of the gas particles with the walls; as a particle is about to hit the container wall, it is “held back”, and its impact is diminished, by the at- tractive forces from surrounding gas particles; this is a pair effect ∼ number of pairs of particles ∼ (n/V )2 = ρ2 P = nRT V −nb −a (n V )2 van der Waals equation a is a material constant; a and b are tabulated for real gases ( P + a V 2 )( V −b ) = RT compare van der Waals equation with virial equation B(T ) = b − a RT PChem I 1.26 How good is the van der Waals model? (V −b)V 2P = RT V 2−a(V −b) V 3 P −V 2bP = RT V 2−aV +ab V 3− ( b + RT P ) V 2+ a P V − ab P = 0 cubic equation ⇒ for fixed T and P , three real roots or one real root and two complex conjugate roots isotherms for the van der Waals equation for ammo- nia PChem I 1.27 between a minimum and a maximum is an inflection point (curvature changes): second derivative vanish- es critical point: at (Tc, Pc, V c) dP dV = 0 and d 2P dV 2 = 0 there are three critical constants, need one more equation: equation of state P = RT V −b − a V 2 (1) dP dV =− RT (V −b)2 + 2a V 3 = 0 at critical point (2) d2P dV 2 = 2RT (V −b)3 − 6a V 4 = 0 at critical point (3) equation (2)⇒ RTc = 2a(V c −b)2 V 3 c (4) PChem I 1.30 insert this result into equation (3) 4a(V c −b)2 V 3 c(V c −b)3 − 6a V 4 c = 0 (5) 2 V c −b − 3 V c = 0 2V c = 3V c −3b ⇒V c = 3b insert into equation (4) RTc = 2a(3b −b)2 (3b)3 = 2a ·4b 2 27b3 Tc = 8a 27bR insert into equation (1) Pc = 8a 27b 3b −b − a 9b2 = 8a 2 ·27b2 − a 9b2 Pc = a 27b2 PChem I 1.31 critical compression factor: Zc = PcV c RTc = a 27b2 ·3b 8a 27b Zc = 3 8 independent of the material constants a and b Z vdWc = 0.375; compare with experimental data range: 0.12 HF – 0.47 N2O4 mode: 0.27; 27% of all organic and inorganic sub- stances have this value of Zc 61% Zc in [0.26, 0.28]; 77% Zc in [0.25, 0.29]; 90% Zc in [0.23, 0.31] van der Waals gas: simple model that captures the essential aspects of real gases critical point is a very characteristic point for real gas- es ⇒ use critical constants as units reduced variables Pr = P Pc , V r = V V c , Tr = T Tc PChem I 1.32
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