UNIT 1
Formula Name |
Equation |
Boyle's Law |
PV = k (N,T) |
Charles's Law |
V/T = k (N,P) |
Avogadro's Law |
V/n = k (T,P) |
Ideal Gas Law |
V = nRT/P or PV = nRT |
Dalton's Law |
Ptotal = P1 + P2 + P3.... |
STP |
1 atm, 0 Celsius |
Gas Density |
d = m/V = PM/RT = N/V |
Partial Pressure |
P1 = X1 * Ptotal |
Root Mean Squared Speed |
v = sqrt(3RT/M) |
Collision Frequency |
f = vrms / mfp (mean free path) |
Average Kinetic Energy |
KE = 3/2 nRT |
Effusion - Graham's Law |
rate1/rate2 = sqrt(MW2/MW1) |
General Rate Law |
rate = k[A]m*[B]n |
Zeroth Order Integrated Rate Law |
[A]t = [A]0 - kt |
First Order Integrated Rate Law |
ln[A]t = ln[A]0 -kt |
Second Order Integrated Rate LAw |
1/[A]t = 1/[A]0 + kt |
Zeroth Order Half Life |
t = [A]0/2k |
First Order Half Life |
t = ln2/k |
Second Order Half Life |
t = 1/k[A]0 |
Arrhenius Equation |
Ae^-Ea/RT |
Logarithmic Form of Arrhenius Equation |
ln(k2/k1) = (-Ea/R) * (1/T2 - 1/T1) |
Michaelis-Menton Enzyme Kinetics |
rate = k2 [E]T [S]/[S] + km |
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UNIT 2
Formula Name/Subject |
Equation/Description |
Equilibrium Constant (concentrations) |
Kc = [products]/[reactants] |
Equilibrium Constant (pressures) |
Kp = P(products)/P(reactants) |
Equilibrium Equation (with rates) |
K = kf/kr |
Q = K |
At equilibirum |
Q < K |
reaction shifts in forward direction |
Q > K |
reaction shifts in reverse direction |
Keq is large (10^3) |
kforward > kreverse |
Keq is small (10^-3) |
kforward < kreverse |
Keq = 1 |
kforward = kreverse |
Kc and Kp Relation |
Kc = Kp * RT^Δn |
L'C: add more reactants |
reaction shifts forward |
L'C: add more products |
reaction shifts reverse |
L'C: increase pressure |
reaction shifts towards fewer moles |
L'C: decrease pressure |
reaction shifts towards greter moles |
L'C: increase volume |
reaction shifts towards greater moles |
L'C: decrease volume |
reaction shifts towards fewer moles |
Endothermic (T) Phase Transitions |
Melting, Sublimation, Evaporation |
Exothermic (P) Phase Transitions |
Freezing, Deposition, Condensation |
Entropy |
S = kB ln(W) |
Change in Entropy for Change in Volume |
ΔS = nR ln(V2/V1) |
Change in Entropy ofSurroundings |
ΔSsurr = -ΔH/T |
Gibbs Free Energy |
ΔG = ΔH - TΔS |
Nonstandard Gibbs Free Energy (1) |
ΔG = ΔG0 + RTlnQ |
Standard Gibbs Free Energy |
ΔG0 = -RTlnK |
Nonstandard Gibbs Free Energy (2) |
ΔG = RT ln(Q/K) |
Clausisus-Claperyon Equation |
ln(P2/P1) = -ΔH/R (1/T2-1/T1) |
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UNIT 3
Formula Name/Info |
Equation/Description |
Molarity (M) |
mol solute/L solution (mol/L) |
Molality (m) |
mol solute/kg solution (mol/kg) |
Mole Fraction (X) |
mol solute/mol solution (mol/mol) |
Vapor Pressure (two volatile chemicals) |
Pvap = PaXa + PbXb |
Boiling Point Elevation |
Tb = kb m i |
Freezing Point Depression |
Tf = -kf m i |
Osmotic Pressure |
pi =iMRT |
Solubility |
S = mol dissolved / L solution |
CIE: add in species already present |
decrease solubility |
Henderson-Hasselbach Equation |
pH = pKa + log(conj. base/acid) |
K value for Neutralization |
Kn = Ka*Kb/Kw |
Equivalence Point |
mol base added = mol acid originally present |
Midpoint |
pH = pKa |
Solvent-Solvent Interactions |
endothermic, overcome IMFs |
Solute-Solute Interactions |
endothermic, overcome IMFs |
Solvent-Solute Interactions |
exothermic, release energy through attractive forces |
To relate Ka to Kb |
Kw = Ka * Kb |
Strong Acids |
H2SO4, HNO3, HCl, HI, HClO4, HClO3, HBr |
Strong Bases |
LiOH, NaOH, KOH, RbOH, CsOH, Ca(OH)2, Sr(OH)2 |
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UNIT 4
Formula Name/Subject |
Equation/Description |
Current (I)) |
charge/time (Amperes) |
Voltage (V) |
energy/charge (Volts) |
Power (W) |
energy/seconds (Watts) |
Oxidation Reaction |
Lose electrons |
Reduction Reaction |
Gain electrons |
Cathode |
Site of reduction, e- flow to cathode |
Anode |
Site of oxidation, e- flow from anode |
Cell Potential (E) |
Ecell = Ecathode + Eanode = Eredcat - Eredan |
Gibbs Free Energy (standard) |
ΔG0 = -nFE0 |
Faraday's Constant |
96,500 C/mol e- |
Nernst Equation |
E = E0 - RT/nF lnQ |
Standard Hydrogen Electrode (SHE) |
2H+ + 2e- -> H2(g) |
Standard Cell Potential |
E0 = RT/nF lnK |
Total Charge (Z) |
Z = I * t (in seconds), in coloumbs |
Moles of Electrons Produced |
n(e-) = Z/F |
Moles of Metal Produced |
n(metal) = n(e-)* mol(metal)/mols e- needed |
Mass of Metal Produced |
m(metal) = n(metal)/MWmetal |
Nernst Equation with pH |
E = E0red + 2.3RT/F logQ |
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