INGENIA

CHM-03

van 't Hoff isochore

ln(K2/K1) = −(ΔH/R)(1/T2 − 1/T1). How K moves with T.

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Equilibriumvan 't Hoff 1884

Governing equation

ln⁡K2K1=−ΔHR(1T2−1T1)\ln\dfrac{K_2}{K_1}=-\dfrac{\Delta H}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right)

T2∈[200,900]T_2 \in \left[200, 900\right]

where

K_1
K at T1 (—)
T_1
T1 (K)
T_2
T2 (K)
\Delta H
Enthalpy of reaction (kJ/mol)
K_2
K at T2 (—)

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CHM-03 · reactor
00:0 / 00:08
①

Governing law — red

ln⁡K2K1=−ΔHR(1T2−1T1)\ln\dfrac{K_2}{K_1}=-\dfrac{\Delta H}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right)

T2∈[200,900]T_2 \in \left[200, 900\right]

T2=200T_2 = 200K2=5.08×10−5K_2 = 5.08\times 10^{-5}

②

Domain of the variable — blue

T_2_{\min} = 200,\quad T_2_{\max} = 900

T2∈[200,900]T_2 \in \left[200, 900\right]

T2=200T_2 = 200T2=200T_2 = 200

③

Response curve — green

ln⁡K2K1=−ΔHR(1T2−1T1)\ln\dfrac{K_2}{K_1}=-\dfrac{\Delta H}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right)

T2∈[200,900]T_2 \in \left[200, 900\right]

T2=200T_2 = 200K2=5.08×10−5K_2 = 5.08\times 10^{-5}

④

Rate of change — amber

dK2dT2\frac{\mathrm{d}K_2}{\mathrm{d}T_2}

T2∈[200,900]T_2 \in \left[200, 900\right]

T2=204.4T_2 = 204.4K2′=1.47×10−5K_2^{\prime} = 1.47\times 10^{-5}

Lecture brief

Historical brief

Ideal-gas law, van ’t Hoff, Nernst, Michaelis–Menten and Clausius–Clapeyron are physical chemistry’s working equations of equilibrium and rate. The lab is pressure, potential and kinetics. This sheet (CHM-03 — van 't Hoff isochore) is the form associated with van 't Hoff 1884. Working symbols: K1K_1, T1T_1, T2T_2, ΔH\Delta H →\rightarrow K2K_2. From d ln K / dT = ΔH / RT² (constant ΔH). Endothermic equilibria heat-shift to the right.

Purpose

Purpose: compute K2K_2 from K1K_1, T1T_1, T2T_2, ΔH\Delta H in Physical chemistry via ln⁡K2K1=−ΔHR(1T2−1T1)\ln\dfrac{K_2}{K_1}=-\dfrac{\Delta H}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right) ln(K2/K1) = −(ΔH/R)(1/T2 − 1/T1). How K moves with T. Use it when a real physical chemistry question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given K1=1.000 —K_1 = 1.000\,\mathrm{—}, T1=298.000 KT_1 = 298.000\,\mathrm{K}, T2=350.000 KT_2 = 350.000\,\mathrm{K}, ΔH=50.000 kJ/mol\Delta H = 50.000\,\mathrm{kJ/mol}, the governing relation ln⁡K2K1=−ΔHR(1T2−1T1)\ln\dfrac{K_2}{K_1}=-\dfrac{\Delta H}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right) yields K2=20.0486 —K_2 = 20.0486\,\mathrm{—}. Constant ΔH between T1 and T2. K1 at T1. Move a slider: the numbers are this situation, not a canned story.

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  • K at T2 K_220.0486 —
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CHM-03 · reactor
00:0 / 00:08

Narration of this film

Constant ΔH between T1 and T2. K1 at T1.

From d ln K / dT = ΔH / RT² (constant ΔH). Endothermic equilibria heat-shift to the right.

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