Liquids and Solids — Comprehensive Notes (Sections 12.1, 12.3–12.5)

Section 12.1 Intermolecular Forces

  • Condensed states are held together by forces called intermolecular forces (IMFs).

  • IMFs are weaker than intramolecular (chemical) bonds but govern physical properties (melting/boiling points, solubility, etc.).

  • Four types of intermolecular forces:

    • Ion–dipole attractions

    • Electrostatic interactions between ions and polar molecules.

    • Hydrated ions form by ion–dipole attractions.

    • Strongest type of IMF.

    • Example: salt water where ionic compounds dissolve in water.

    • Hydrogen bonds

    • Require two components:

      • A molecule with a partially positive hydrogen atom (a hydrogen donor).

      • A molecule with a partially negative N, O, or F atom (a hydrogen acceptor).

    • An attraction between the partially positive H in one molecule and the lone pair on N, O, or F in another molecule.

    • Dipole–dipole interactions (permanent dipole–dipole)

    • Polar molecules interact with other polar molecules via electrostatic attractions between oppositely charged ends.

    • London dispersion forces (dispersion forces)

    • Result from instantaneous dipoles due to random electron motion.

    • Induced dipoles in neighboring molecules lead to short-lived attractions.

  • Intramolecular vs Intermolecular Forces

    • Intramolecular forces occur within a molecule (covalent or ionic bonds); relatively strong and remain after physical processes.

    • Intermolecular forces occur between molecules; relatively weaker and are affected by physical processes (e.g., heating, phase changes).

  • Polar vs. non-polar molecules

    • Polar molecules have a permanent dipole moment (uneven charge distribution).

    • Non-polar molecules have no permanent dipole moment (even charge distribution).

  • Halogen size and polarizability (data related to IMFs)

    • Atomic Radius (pm) and Boiling Point (K) for halogens:

    • Fluorine: extRadius=60extpm,extBP=85extKext{Radius} = 60 ext{ pm}, ext{ BP} = 85 ext{ K}

    • Chlorine: extRadius=100extpm,extBP=239extKext{Radius} = 100 ext{ pm}, ext{ BP} = 239 ext{ K}

    • Bromine: extRadius=117extpm,extBP=332extKext{Radius} = 117 ext{ pm}, ext{ BP} = 332 ext{ K}

    • Iodine: extRadius=136extpm,extBP=457extKext{Radius} = 136 ext{ pm}, ext{ BP} = 457 ext{ K}

  • Types of Intermolecular Forces (Summary)

    • Strongest → Weakest order (conceptual):

    • Ion–dipole attractions (present in mixtures of ionic and polar compounds, e.g., NaCl dissolved in water).

    • Hydrogen bonding (between molecules containing H–donor and H–acceptor N, O, or F).

    • Dipole–dipole attractions (polar molecules, e.g., H2O, HCl).

    • London dispersion forces (all molecular substances and inert gases; e.g., H2O, HCl, Cl2, He, Ne).

Section 12.3 Phase Changes and Heating Curves

  • Phase changes and related terms:

    • Melting (fusion): solid → liquid

    • Freezing (solidification): liquid → solid

    • Vaporization (evaporation): liquid → gas

    • Condensation: gas → liquid

    • Sublimation: solid → gas

    • Deposition: gas → solid

  • Enthalpies associated with phase changes (per mole):

    • <br>ΔHextvap(enthalpy of vaporization): energy to vaporize 1 mol of a liquid<br><br>\Delta H_{ ext{vap}}\,\text{(enthalpy of vaporization)}: \text{ energy to vaporize 1 mol of a liquid}<br>

    • ΔHextfus(enthalpy of fusion): energy to melt 1 mol of a solid<br>\Delta H_{ ext{fus}}\,\text{(enthalpy of fusion)}: \text{ energy to melt 1 mol of a solid}<br>

    • ΔHextsub(enthalpy of sublimation): energy to sublime 1 mol of a solid<br>\Delta H_{ ext{sub}}\,\text{(enthalpy of sublimation)}: \text{ energy to sublime 1 mol of a solid}<br>

  • Heating curve (for a pure substance)

    • Temperature versus time as a substance is heated.

    • Plateaus occur at phase changes due to latent heat (no temperature change while changing phase).

  • Examples and calculations:

    • Problem: Identify the phase change for each equation:

    • (a) \ce{C{18}H{38}(s) -> C{18}H{38}(l)}

      • Melting (fusion).

    • (b) \ce{CO2(g) -> CO2(s)}

      • Deposition.

    • (c) \ce{NH3(l) -> NH3(g)}

      • Vaporization (boiling/evaporation).

    • Example: Energy required to melt 16.4 g of ice at 0°C with ΔHfus=6.01 kJmol1\Delta H_{\text{fus}} = 6.01\ \text{kJ}\,\text{mol}^{-1}

    • Molar mass of water: M_{\ce{H2O}} = 18.015\ \text{g}\,\text{mol}^{-1}

    • Moles melted: n=mM=16.4 g18.015 g mol10.9105 moln = \frac{m}{M} = \frac{16.4\ \text{g}}{18.015\ \text{g mol}^{-1}} \approx 0.9105\ \text{mol}

    • Energy: q=nΔHfus=(0.9105)(6.01 kJ mol1)5.47 kJq = n \Delta H_{\text{fus}} = (0.9105) (6.01\ \text{kJ mol}^{-1}) \approx 5.47\ \text{kJ}

Section 12.4 Vapor Pressure, Boiling Point, and the Clausius–Clapeyron Equation

  • Vapor pressure ( Pvap )

    • The equilibrium pressure of a vapor above its liquid or solid in a closed container.

    • At equilibrium, rate of evaporation equals rate of condensation.

    • Pvap increases with temperature; it is a function of intermolecular forces.

  • Boiling point (BP)

    • The temperature at which Pvap equals the ambient atmospheric pressure (P_{ ext{atm}}).

    • Example reference points for water at various elevations:

    • Sea level: BP = 100ext°C100^ ext{°}C

    • Everest: BP ≈ 69.9ext°C69.9^ ext{°}C

  • Relationship among Pvap, BP, and IMFs

    • Substances with stronger IMFs tend to have lower Pvap at a given temperature and higher BP.

    • The Pvap–T curves differ for substances (e.g., diethyl ether, ethanol, water) due to IMF strength.

  • Clausius–Clapeyron equation (to relate Pvap at two temperatures)

    • General form (two states):
      ln(P<em>2P</em>1)=ΔH<em>extvapR(1T</em>21T1)\ln\left(\frac{P<em>2}{P</em>1}\right) = -\frac{\Delta H<em>{ ext{vap}}}{R}\left( \frac{1}{T</em>2} - \frac{1}{T_1} \right)

    • Alternative linear form: lnP=ΔHextvapR1T+C\ln P = -\frac{\Delta H_{ ext{vap}}}{R}\frac{1}{T} + C where C is a constant.

    • Universal gas constant: R=8.314 J mol1K1R = 8.314\ \text{J mol}^{-1} \text{K}^{-1}

    • In practice, use Pvap data at known temperatures to solve for ΔHextvap\Delta H_{ ext{vap}} or to predict Pvap at another temperature.

  • Example: Methanol

    • Given: Normal boiling point T<em>1=64.60C=337.75 KT<em>1 = 64.60^{\circ}\text{C} = 337.75\ \text{K}; ΔH</em>vap=35.2 kJ mol1=35200 J mol1\Delta H</em>{\text{vap}} = 35.2\ \text{kJ mol}^{-1} = 35200\ \text{J mol}^{-1}; Measured vapor pressure at T<em>2=25.00C=298.15 KT<em>2 = 25.00^{\circ}\text{C} = 298.15\ \text{K}; Assume P</em>1=1 atm=760 torrP</em>1 = 1\ \text{atm} = 760\ \text{torr}.

    • Calculation steps:

    • ln(P<em>2P</em>1)=ΔH<em>vapR(1T</em>21T1)\ln\left(\frac{P<em>2}{P</em>1}\right) = -\frac{\Delta H<em>{\text{vap}}}{R}\left( \frac{1}{T</em>2} - \frac{1}{T_1} \right)

    • Compute: ΔHvapR=352008.3144237.5\frac{\Delta H_{\text{vap}}}{R} = \frac{35200}{8.314} \approx 4237.5

    • 1T<em>21T</em>1=1298.151337.750.000391 K1\frac{1}{T<em>2} - \frac{1}{T</em>1} = \frac{1}{298.15} - \frac{1}{337.75} \approx 0.000391\ \text{K}^{-1}

    • Product: 4237.5×0.0003911.6564237.5 \times 0.000391 \approx 1.656

    • ln(P2760)1.656\ln\left(\frac{P_2}{760}\right) \approx -1.656

    • P2760e1.6560.191\frac{P_2}{760} \approx e^{-1.656} \approx 0.191

    • P20.191×760145 torrP_2 \approx 0.191 \times 760 \approx 145\ \text{torr}

    • Result: The vapor pressure of methanol at 25C25^{\circ}\text{C} is approximately P21.45×102 torrP_2 \approx 1.45\times 10^{2}\ \text{torr}.

  • Applications and notes

    • The Clausius–Clapeyron equation enables extraction of enthalpies from Pvap data and vice versa.

    • Pvap data and BP are practical indicators of how substances will behave under heating, cooling, or reduced/augmented pressure conditions.

Section 12.5 Phase Diagrams

  • Phase diagrams show the phase (solid, liquid, gas) of a substance under all possible pressure–temperature (P–T) combinations.

  • Key features of a generic phase diagram:

    • Regions corresponding to solid, liquid, and gas phases.

    • Lines separating phases depict equilibria between phases (fusion/melting line, vaporization/condensation line, sublimation/deposition line).

    • Points of interest:

    • Triple point: the single point where all three phases are in equilibrium; lines intersect there.

    • Critical point: above this P–T location, the substance no longer exists as a distinct liquid; liquid and gas become indistinguishable (supercritical fluid).

    • Normal melting point: the temperature at which the solid melts at 1 atm.

    • Normal boiling point: the temperature at which the vapor pressure equals 1 atm.

  • Reading and interpreting phase diagrams

    • Identify phase in each region (solid, liquid, gas).

    • Determine the phase boundary for solid–gas equilibrium (sublimation/deposition line).

    • Locate the normal boiling point on the temperature axis by finding the point where Pvap equals 1 atm.

  • Conceptual use

    • Phase diagrams predict phase changes when changing temperature or pressure (
      e.g., heating/cooling at constant pressure or compression/expansion at constant temperature).

  • Example interpretation task (from slides)

    • a) Identify the phase(s) in regions A, B, and C.

    • b) Identify the line where the solid and gas phases are in equilibrium (sublimation line).

    • c) Identify the point indicating the normal boiling point (where Pvap = 1 atm).

    • Note: The exact labels A, B, C depend on the specific diagram provided, but the concepts remain the same.