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First Law of Thermodynamics

Shaun Williams, PhD

Work and Heat

James P. Joule (1818-1889)

  • Joule was one of the pioneers of modern thermodynamics.
  • Among his experiments, Joule attempted to measure the effect of work on the temperature of water.
Joule's apparatus consisted of fan blades attached to a center rod which could be rotated.

The First Law of Thermodynamics

The capacity of a system to do work is increased by heating the system or doing work on it.

Heat

Example 3.1

How much energy is needed to raise the temperature of \(5.0\, g\) of water from \(21.0^\circ C\) to \(25.0^\circ C\)?

Side Note: Partial Derivative

Work

Type of Work Displacement Resistance \(dw=\)
Expansion \( dV \) (volume) \( -P_{ext} \) (pressure) \( -P_{ext}\,dV \)
Electrical \( dQ \) (charge) \( -W \) (resistance) \( -W\,dQ \)
Extension \( dL \) (length) \( T \) (tension) \( T\,dL \)
Stretching \( dA \) \( s \) (surface tension) \( s\,dA \)

Example 3.2

What is the work done by \( 1.00\, mol\) of an ideal gas expanding from a volume of \( 22.4\, L \) to a volume of \( 44.8\, L \) against a constant external pressure of \( 0.500\, atm \)?

Reversible and Irreversible Pathways

Reversible Gas Expansions

Solving Reversible Gas Expansion

\( dw = -P_{ext}\, dV = -P\, dV \)

\[ \begin{eqnarray} w &=& - \int P\,dV \\ &=& -\int \left(\frac{nRT}{V}\right) \\ &=& -nRT \int_{V_1}^{V_2} \frac{dV}{V} = -nRT \ln \left(\frac{V_2}{V_1}\right) \end{eqnarray} \]

Example 3.3

What is the work done by \( 1.00\, mol \) of an ideal gas expanding reversibly from a volume of \( 22.4\, L \) to a volume of \( 44.8\, L \) at a constant temperature of \( 273\, K \)?

The area under the curve of pressure versus volume is the work done during the expansion or contraction.

Note: Isothermal Processes of an Ideal Gas

Constant Volume "Expansion" - Isochoric

Example 3.4

Consider \(1.00\, mol\) of an ideal gas with \( C_V=\frac{3}{2}R \) that undergoes a temperature change from \(125\, K\) to \(255\, K\) at a constant volume of \( 10.0\, L\). Calculate \(\Delta U\), \(q\), and \(w\) for this change.

Constant Pressure Pathway - Isobaric

Reversible Isobaric Changes

\( dH = dq-P\,dV+P\,dV+V\,dP=dq+V\,dP \)

Example 3.5

Consider \(1.00\,mol\) of an ideal gas with \(C_P=\frac{5}{2}R\) that changes from temperature from \(125\,K\)to \(255\,K\) at a constant pressure of \(10.0\,atm\). Calculate \(\Delta U\), \(\Delta H\), \(q\) and \(w\) for this change.

Example 3.6

Calculate \(q\), \(w\), \(\Delta U\), and \(\Delta H\) for \(1.00\,mol\) of an ideal gas expanding reversibly and isothermally at \(273\,K\) from a volume of \(22.4\,L\) and a pressure of \(1.00\,atm\) to a volume of \(44.8\,L\) and a pressure of \(0.500\,atm\).

Adiabatic Pathways

Reversible Adiabatic Expansion of an Ideal Gas

We know that \[ dw=-P\,dV \] and \[ dw=nC_V\,dT \] therefore \[ -P\,dV = nC_V\,dT \] Using the ideal gas law we find that \[ -\frac{nRT}{V}\,dV = n C_V\,dT \]

Reversible Adiabatic Expansion Continued

\[ -\frac{nRT}{V}\,dV = n C_V\,dT \] Integrating to get to macroscopic changes \[ \int_{V_1}^{V_2}\frac{dV}{V}=-\frac{C_V}{R}\int_{T_1}^{T_2}\frac{dT}{T} \] which solves to \[ \ln\left( \frac{V_2}{V_1} \right) = -\frac{C_V}{R} \ln \left( \frac{T_2}{T_1} \right) \] \[ \left( \frac{V_2}{V_1} \right) = \left( \frac{T_2}{T_1} \right)^{-\frac{C_V}{R}} \Rightarrow T_1 \left(\frac{V_2}{V_1}\right)^{-\frac{R}{C_V}}=T_2 \]

Example 3.7

\(1.00\,mol\) of an ideal gas (\(C_V=\bfrac{3}{2}R\)) initially occupies \(22.4\,L\) at \(273\,K\). The gas expands adiabatically and reversibly to a final volume of \(44.8\,L\). Calculate \(\Delta T\), \(q\), \(w\), \(\Delta U\), and \(\Delta H\) for the expansion.

Thermodynamic Properties for a Reversible Expansion or Compression

Pathway     \(q\)      \(w\)      \(\Delta U\)     \(\Delta H\)
Isothermal \(nRT\ln\frac{V_2}{V_1}\)   \(-nRT\ln\frac{V_2}{V_1}\)   \(0\) \(0\)
Isochoric \(C_V\,\Delta T\) \(0\) \(C_V\,\Delta T\) \(\begin{eqnarray} &C_V&\,\Delta T \\ &&+V\,\Delta P\end{eqnarray}\)
Isobaric \(C_P\,\Delta T\) \(-P\,\Delta V\) \(\begin{eqnarray} &C_P&\,\Delta T\\ &&-P\,\Delta V\end{eqnarray}\) \(C_P\,\Delta T\)
Adiabatic \(0\) \(C_V\,\Delta T\) \(C_V\,\Delta T\) \(C_P\,\Delta T\)

Calorimetry

Generic schematic of a calorimeter in which heat is leaving the reaction and entering the surrounding and the temperature of the surroundings is monitored with a thermometer.

Bomb Calorimetry

Generic schematic of a bomb calorimeter.

"Water Equivalent" of a Bomb Calorimeter

Using the "Water Equivalent"

Example 3.8

A student burned a \(0.7842\, g\) sample of benzoic acid (\(C_7H_6O_2\)) in a bomb calorimeter initially at \(25.0^\circ C\) and saw a temperature increase of \( 2.02^\circ C\). She then burned a \( 0.5348\, g\) sample of naphthalene (\(C_{10}H_8\)) (again from an initial temperature of \(25^\circ C\)) and saw a temperature increase of \( 2.24^\circ C\). From this data, calculate \(\Delta H_c\) for naphthalene (assuming \( e_{wire} \) and \( e_{other} \) are unimportant.)

Temperature Dependence of Enthalpy

Varying Heat Capacity

Empirical Parameters for the Temperature Dependence of \(C_p\)

Substance \(a\,(J\,mol^{-1}\,K^{-1})\) \(b\,(J\,mol^{-1}\,K^{-2})\) \(c\,(J\,mol^{-1}\,K)\)
\(C(gr)\) \(16.86\) \(4.77\times 10^{-3}\) \(-8.54\times 10^5\)
\(CO_2(g)\) \(44.22\) \(8.79\times 10^{-3}\) \(-8.62\times 10^5\)
\(H_2O(l)\) \(75.29\) \(0\) \(0\)
\(N_2(g)\) \(28.58\) \(3.77\times 10^{-3}\) \(-5.0\times 10^4\)
\(Pb(s)\) \(22.13\) \(1.172\times 10^{-2}\) \(9.6\times 10^4\)

Example 3.9

What is the molar enthalpy change for a temperature increase from \(273\, K\) to \(353\, K\) for \(Pb(s)\)?

Example 3.10

The enthalpy of formation of \( NH_3(g) \) is \( -46.11\,\bfrac{kJ}{mol} \) at \( 25^\circ C\). Calculate the enthalpy of formation at \( 100^\circ C \). Assuming heat capacities are independent of temperature.

Substance \(C_p\,(J\,mol^{-1}\,K^{-1})\)
\(N_2(g)\) \(29.12\)
\(H_2(g)\) \(28.82\)
\(NH_3(g)\) \(35.06\)

Reaction Enthalpies

Example 3.11

Find \(\Delta H_{rxn}\) for the reaction \[ 2CO(g) + O_2(g) \rightarrow 2CO_2(g) \] given that \[ C(gr)+\frac{1}{2}O_2(g) \rightarrow CO(g) \;\;\; \Delta H = -110.53\,kJ \] \[ C(gr)+O_2(g) \rightarrow CO_2(g) \;\;\; \Delta H = -393.51\,kJ \]

Standard Enthalpy of Formation

The standard state of a substance is the most stable form of that substance at 1 atmosphere pressure and the specified temperature.

Standard Formation Reactions

Alternation Use of Heats of Formation

Ionization Reactions

Average Bond Enthalpies

Example 3.12

Estimate the reaction enthalpy for the combustion of ethanol \[ C_2H_5OH(g) + O_2(g) \rightarrow 2CO_2(g) + H_2O(g) \] using

Bond      Average Bond Energy (kJ/mol)
C-H 413
C-C 348
C-O 358
O=O 495
C=O 799
O-H 463

The Born-Haber Cycle

Example 3.13

Find \(\Delta H_f\) for \(KBr\) given the following data: \[ \begin{eqnarray} K(s)\rightarrow K(g) &\;\;\;& \Delta H_{sub}(K)=89\bfrac{kJ}{mol} \\ Br_2(l)\rightarrow Br_2(g) &\;\;\;& \Delta H_{vap}=31\bfrac{kJ}{mol} \\ Br_2(g)\rightarrow 2Br(g) &\;\;\;& D(Br-Br)=193\bfrac{kJ}{mol} \\ K(g)\rightarrow K^+(g)+e^- &\;\;\;& 1^{st}IP(K)=419\bfrac{kJ}{mol} \\ Br(g) + e^-\rightarrow Br^-(g) &\;\;\;& 1^{st}EA(Br)=194\bfrac{kJ}{mol} \\ K^+(g) + Br^-(g) \rightarrow KBr(s) &\;\;\;& \Delta H_{lat}(KBr)=675\bfrac{kJ}{mol} \end{eqnarray} \]

Born-Haber Cycle Graphically

A diagram that uses arrows to show each step of the Born-Haber cycle for sodium chloride that was described on the previous slide.

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