Peter Atkins • Julio de Paula Atkins’ Physical Chemistry Eighth Edition Chapter 2 – Lecture 4 The First Law Copyright © 2006 by Peter Atkins and Julio de Paula State Functions and Exact Differentials • State function – state of the system independent of manner and time to prepare • Path functions – processes that describe prep of the state • e.g., Heat, work, temperature • Systems do not possess heat, work, or temperature • Advantage of state functions: • Can combine measurements of different properties to obtain value of desired property Fig 2.20 As V and T change, the internal energy, U changes non-adiabatic adiabatic When the system completes the path: f ΔU dU i dU is said to be: an exact differential f q dq i,path q is said to be: an inexact differential Fig 2.21 The partial derivative (∂U/∂V)T is the slope of U w.r.t V at constant T Fig 2.22 The partial derivative (∂U/∂T)V is the slope of U w.r.t T at constant V Fig 2.23 The overall change in U (i.e. dU) which arises when both V and T change U U dU dV dT V T T V The full differential of U w.r.t V and T Partial derivatives representing physical properties: U Constant volume heat capacity C V T V H Constant pressure heat capacity CP T P Internal pressure U πT V T Fig 2.24 The internal pressure πT is the slope of U w.r.t. V at constant T has dimensions of pressure Partial derivatives representing physical properties: U Constant volume heat capacity C V T V H Constant pressure heat capacity CP T P Internal pressure Now: U πT V T U U dU dV dT π T dV C V dT V T T V Fig 2.25 For a perfect gas the internal energy is independent of volume at constant temperature Two cases for real gases: U πT 0 V T Fig 2.26 Schematic of Joule’s attempt to measure ΔU for an isothermal expansion of a gas q absorbed by gas ∝ T U πT V T • For expansion into vacuum, w=0 • No ΔT was observed, so q = 0 at 22 atm • In fact, experiment was crude and did not detect the small ΔT Changes in Internal Energy at Constant Pressure • Partial derivatives useful to obtain a property that cannot be observed directly: • e.g., dU π T dV CV dT • Dividing through by dT: U V πT CV T P T P 1 V • Where α expansion coefficient V T P 1 V isothermal compressibility • and κ T V P T Changes in Internal Energy at Constant Pressure 1 V Substituting: α V T P Into: U π T V C V T P T P Gives: U απ V C T V T P For a perfect gas: U CV T P 1 V κT V P T Changes in Internal Energy at Constant Pressure • May also express the difference in heat capacities with observables: • Cp – Cv = nR H U CP C V T P T P • Since H = U + PV = U + nRT U H CP C V nR nR T P T P • And: α 2 TV CP C V κT