Portal:Chemistry/Useful equations and links

Note: I am developing this page as a study aid for myself. I may later find a home for it at the chemistry portal or at Wikibooks or Wikiversity. Shalom (HelloPeace) 00:18, 4 November 2007 (UTC)

Chemical elements

Ions

Gases

:Main article: Gas laws

=Ideal gas law =

:\frac {P_1V_1} {T_1} = \frac {P_2V_2} {T_2}.

:PV = nRT \,,

where

:P is the pressure (SI unit: pascal)

:V is the volume (SI unit: cubic metre)

:n is the number of moles of gas

:R is the ideal gas constant (SI: 8.3145 J/(mol K))

:T is the thermodynamic temperature (SI unit: kelvin).

An equivalent formulation of this law is:

:PV = NkT \,

where

:N is the number of molecules

:k is the Boltzmann constant.

= Graham's Law =

:{\mbox{Rate}_1 \over \mbox{Rate}_2}=\sqrt{M_2 \over M_1}

where:

:Rate1 is the rate of effusion of the first gas.

:Rate2 is the rate of effusion for the second gas.

:M1 is the molar mass of gas 1

:M2 is the molar mass of gas 2.

= Kinetic theory =

:P = {Nmv_{rms}^2 \over 3V}

Also, as Nm is the total mass of the gas, and mass divided by volume is density

: P = {1 \over 3} \rho\ v_{rms}^2

where ρ is the density of the gas.

This result is interesting and significant, because it relates pressure, a macroscopic property, to the average (translational) kinetic energy per molecule (1/2mvrms2), which is a microscopic property.

The root mean square velocity of a molecule is

:v_{rms}^2 = \frac{3RT}{\mbox{molar mass}}

with v in m/s, T in kelvins, and R is the gas constant. The molar mass is given as kg/mol.

= Dalton's Law =

The pressure of a mixture of gases can be defined as the summation


:P_{total} = \sum_{i=1} ^ n {p_i}       or      P_{total} = p_1 +p_2 + \cdots + p_n


where p_{1},\ p_{2},\ p_{n} represent the partial pressure of each component.

It is assumed that the gases do not react with each other.

:\ P_{i} =P_{total}m_i

where m_i\ = the mole fraction of the i-the component in the total mixture of m components .

= Van der Waals equation =

:\left(p + \frac{n^2 a}{V^2}\right)\left(V-nb\right) = nRT,

where

:p is the pressure of the fluid

:V is the total volume of the container containing the fluid

:a is a measure of the attraction between the particles a=N_\mathrm{A}^2 a'

:b is the volume excluded by a mole of particles \, b=N_\mathrm{A} b'

:n is the number of moles

:R is the gas constant, \,R= N_\mathrm{A} k

Solutions

The partition coefficient is the ratio of concentrations of un-ionized compound between the two solutions. To measure the partition coefficient of ionizable solutes, the pH of the aqueous phase is adjusted such that the predominant form of the compound is un-ionized. The logarithm of the ratio of the concentrations of the un-ionized solute in the solvents is called log P:

:* log\ P_{oct/wat} = log\Bigg(\frac{\big[solute\big]_{octanol}}{\big[solute\big]_{water}^{un-ionized}}\Bigg)


= Equilibrium =

Electrochemistry

Isomerism

= Chirality =

Analytical chemistry

Spectroscopy

Nuclear chemistry

= Radiocarbon dating =

The radioactive decay of carbon-14 follows an exponential decay.

A quantity is said to be subject to exponential decay if it decreases at a rate proportional to its value. Symbolically, this can be expressed as the following differential equation, where N is the quantity and λ is a positive number called the decay constant:

:\frac{dN}{dt} = -\lambda N.

The solution to this equation is:

:N = N_0e^{-\lambda t}\,,

where, for a given sample of carbonaceous matter:

:N_0 = number of radiocarbon atoms at t = 0, i.e. the origin of the disintegration time,

:N = number of radiocarbon atoms remaining after radioactive decay during the time t,

:{\lambda} = radiocarbon decay or disintegration constant.

:Two related times can be defined:

:*mean- or average-life: mean or average time each radiocarbon atom spends in a given sample until it decays.

:*half-life: time lapsed for half the number of radiocarbon atoms in a given sample, to decay,

It can be shown that:

:t_{avg} \, = \frac{1}{\lambda} = radiocarbon mean- or average-life = 8033 years (Libby value)

:t_\frac{1}{2} \, = t_{avg} \cdot \ln 2 = radiocarbon half-life = 5568 years (Libby value)

Notice that dates are customarily given in years BP which implies t(BP) = -t because the time arrow for

dates runs in reverse direction from the time arrow for the corresponding ages. From these considerations and the above equation, it results:

For a raw radiocarbon date:

:t(BP) = \frac{1}{\lambda} {\ln \frac{N}{N_0}}

and for a raw radiocarbon age:

:t(BP) = -\frac{1}{\lambda} {\ln \frac{N}{N_0}}

Thermodynamics

= Laws of thermodynamics =

:* Zeroth law of thermodynamics

:*:A \sim B \wedge B \sim C \Rightarrow A \sim C

:* First law of thermodynamics

:*:\mathrm{d}U=\delta Q-\delta W\,

:* Second law of thermodynamics

:*:\oint \frac{\delta Q}{T} \ge 0

:* Third law of thermodynamics

:*: T \rightarrow 0, S \rightarrow C

= Identities =

Chemical thermodynamics studies PV work, which occurs when the volume of a fluid changes. PV work is represented by the following differential equation:

:dW = -P dV \,

where:

  • W = work done on the system
  • P = external pressure
  • V = volume

Therefore, we have:

:W=-\int_{V_i}^{V_f} P\,dV

Clausius defined the change in entropy ds of a thermodynamic system, during a reversible process, as

:dS = \frac{\delta Q}{T} \!

where

: δQ is a small amount of heat introduced to the system,

: T is a constant absolute temperature

Note that the small amount \delta Q of energy transferred by heating is denoted by \delta Q rather than dQ, because Q is not a state function while the entropy is.

The function H was introduced by the Dutch physicist Heike Kamerlingh Onnes in early 20th century in the following form:

:H = E + pV,\,

where E represents the energy of the system. In the absence of an external field, the enthalpy may be defined, as it is generally known, by:

:H = U + pV,\,

The internal energy is essentially defined by the first law of thermodynamics which states that energy is conserved:

: \Delta U = Q + W + W' \,

where

U is the change in internal energy of a system during a process.

:Q is heat added to a system (measured in joules in SI); that is, a positive value for Q represents heat flow into a system while a negative value denotes heat flow out of a system.

:W is the mechanical work done on a system (measured in joules in SI)

: W' is energy added by all other processes

Although the internal energy is not exactly measurable, it may be expressed in terms of other similarly unmeasurable quantities. Using the above two equations in the first law of thermodynamics to construct one possible expression for the internal energy of a closed system gives:

:\mathrm{d}U = \delta Q - d W = T\mathrm{d}S-p\mathrm{d}V\,

:\Delta G = \Delta H - T \Delta S \, for constant temperature

:\Delta G^\circ = -R T \ln K \,

:\Delta G = \Delta G^\circ + R T \ln Q \,

:\Delta G = -nF \Delta E \,

and rearranging gives

:nF\Delta E^\circ = RT \ln K \,

:nF\Delta E = nF\Delta E^\circ - R T \ln Q \, \,

:\Delta E = \Delta E^\circ - \frac{R T}{n F} \ln Q \, \,

which relates the electrical potential of a reaction to the equilibrium coefficient for that reaction.

where

ΔG = change in Gibbs free energy, ΔH = change in enthalpy, T = absolute temperature, ΔS = change in entropy, R = gas constant, ln = natural logarithm, K = equilibrium constant, Q = reaction quotient, n = number of electrons per mole product, F = Faraday constant (coulombs per mole), and ΔE = electrical potential of the reaction. Moreover, we also have:

:K_{eq}=e^{- \frac{\Delta G^\circ}{RT}}

:\Delta G^\circ = -RT(\ln K_{eq}) = -2.303RT(\log K_{eq})

which relates the equilibrium constant with Gibbs free energy.

The Helmholtz energy is defined as:

:A \equiv U-TS\,Levine, Ira. N. (1978). "Physical Chemistry" McGraw Hill: University of Brooklyn

From the first law of thermodynamics we have:

: {\rm d}U = \delta Q - \delta W\,

where U is the internal energy, \delta Q is the energy added by heating and \delta W=p{\rm d}V is the work done by the system. From the second law of thermodynamics, for a reversible process we may say that \delta Q=T{\rm d}S. Differentiating the expression for A  we have:

:{\rm d}A = {\rm d}U - (T{\rm d}S + S{\rm d}T)\,

:= (T{\rm d}S - p\,{\rm d}V) - T{\rm d}S - S{\rm d}T\,

:= - p\,{\rm d}V - S{\rm d}T\,

= Maxwell relations =

The four most common Maxwell relations are the equalities of the second derivatives of each of the four thermodynamic potentials, with respect to their thermal natural variable (temperature T  or entropy S ) and their mechanical natural variable (pressure p  or volume V ):

:

\left(\frac{\partial T}{\partial V}\right)_S =

-\left(\frac{\partial p}{\partial S}\right)_V\qquad=

\frac{\partial^2 U }{\partial S \partial V}

:

\left(\frac{\partial T}{\partial p}\right)_S =

+\left(\frac{\partial V}{\partial S}\right)_p\qquad=

\frac{\partial^2 H }{\partial S \partial p}

:

\left(\frac{\partial S}{\partial V}\right)_T =

+\left(\frac{\partial p}{\partial T}\right)_V\qquad= -

\frac{\partial^2 A }{\partial T \partial V}

:

\left(\frac{\partial S}{\partial p}\right)_T =

-\left(\frac{\partial V}{\partial T}\right)_p\qquad=

\frac{\partial^2 G }{\partial T \partial P}

where the potentials as functions of their natural thermal and mechanical variables are:

:U(S,V)\, - The internal energy

:H(S,p)\, - The Enthalpy

:A(T,V)\, - The Helmholtz free energy

:G(T,p)\, - The Gibbs free energy

= Boltzmann distribution =

In physics, the Boltzmann distribution predicts the distribution function for the fractional number of particles Ni / N occupying a set of states i which each respectively possess energy Ei:

:{{N_i}\over{N}} = {{g_i e^{-E_i/k_BT}}\over{Z(T)}}

where k_B is the Boltzmann constant, T is temperature (assumed to be a sharply well-defined quantity), g_i is the degeneracy, or number of states having energy E_i, N is the total number of particles:

:N=\sum_i N_i\,

and Z(T) is called the partition function, which can be seen to be equal to

:Z(T)=\sum_i g_i e^{-E_i/k_BT}.

Chemical kinetics

border="1" cellpadding="4" cellspacing="0"

!

!Zero Order

!First Order

!Second Order

!n-th Order

Rate Law

|-\frac{d[A]}{dt} = k

|-\frac{d[A]}{dt} = k[A]

|-\frac{d[A]}{dt} = k[A]^2

|-\frac{d[A]}{dt} = k [A]^n

Integrated Rate Law

|\ [A] = [A]_0 - kt

|\ [A] = [A]_0 e^{-kt}

|\frac{1}{[A]} = \frac{1}{[A]_0} + kt

|\frac{1}{[A]^{n-1}} = \frac{1}{{[A]_0}^{n-1}} + (n-1)kt

[Except first order]

Units of Rate Constant \ k

|\frac{M}{s}

|\frac{1}{s}

|\frac{1}{M \cdot s}

|\frac{1}{M^{n-1} \cdot s}

Linear Plot to determine \ k

|[A] \ \mbox{vs.} \ t

|\ln ([A]) \ \mbox{vs.} \ t

|\frac{1}{[A]} \ \mbox{vs.} \ t

|\frac{1}{[A]^{n-1}} \ \mbox{vs.} \ t

[Except first order]

Half-life

|t_{1/2} = \frac{[A]_0}{2k}

|t_{1/2} = \frac{\ln (2)}{k}

|t_{1/2} = \frac{1}{[A]_0 k}

|t_{1/2} = \frac{2^{n-1}-1}{(n-1)k[A_0]^{n-1}}

[Except first order]

It can be shown that, for exponential decay, the half-life t_{1/2} obeys this relation:

:

t_{1/2} = \frac{\ln (2)}{\lambda}

where

:* \ln (2) is the natural logarithm of 2 (approximately 0.693), and

:* λ is the decay constant, a positive constant used to describe the rate of exponential decay.

The half-life is related to the mean lifetime τ by the following relation:

: t_{1/2} = \ln (2) \cdot \tau

In short, the Arrhenius equation is an expression that shows the dependence of the rate constant k of chemical reactions on the temperature T (in Kelvin) and activation energy Ea, as shown below:[http://www.iupac.org/goldbook/A00102.pdf Arrhenius activation energy] - IUPAC Goldbook definition

:k = A e^{{-E_a}/{RT}}

where A is the pre-exponential factor or simply the prefactor and R is the gas constant.

Chromatography

The Van Deemter equation for the plate height (H) is:

: H = A + \frac{B}{u} + C \cdot u

Where

A is equal to the multiple paths taken by the chemical compound, in open tubular capillaries this term will be zero as there are no multiple paths. The multiple paths occur in packed columns where several routes through the column packing, which results in band spreading.

B/u is equal to the longitudinal diffusion of the particles of the compound.

Cu is equal to the equilibration point. In a column, there is an interaction between the mobile and stationary phases, Cu accounts for this.

Electronic transitions

:\frac{1}{\lambda_{\mathrm{vac}}} = R_{\mathrm{H}} \left(\frac{1}{n_1^2}-\frac{1}{n_2^2}\right)

Where

:\lambda_{\mathrm{vac}} is the wavelength of the light emitted in vacuum,

:R_{\mathrm{H}} is the Rydberg constant for hydrogen,

:n_1 and n_2 are integers such that n_1 < n_2,

By setting n_1 to 1 and letting n_2 run from 2 to infinity, the spectral lines known as the Lyman series converging to 91nm are obtained, in the same manner:

n_1 n_2 Name Converge toward
1 2 \rightarrow \infty Lyman series 91.13 nm
2 3 \rightarrow \infty Balmer series 364.51 nm
3 4 \rightarrow \infty Paschen series 820.14 nm
4 5 \rightarrow \infty Brackett series 1458.03 nm
5 6 \rightarrow \infty Pfund series 2278.17 nm
6 7 \rightarrow \infty Humphreys series 3280.56 nm

The Lyman series is in the ultraviolet while the Balmer series is in the visible and the Paschen, Brackett, Pfund, and Humphreys series are in the infrared.

Quantum mechanics

The same separation of variables technique can be applied to the three-dimensional case to give the energy eigenfunctions:

:\psi_{n_x,n_y,n_z} = \sqrt{\frac{8}{L_x L_y L_z}} \sin \left( \frac{n_x \pi x}{L_x} \right) \sin \left( \frac{n_y \pi y}{L_y} \right) \sin \left( \frac{n_z \pi z}{L_z} \right) \quad (22)

:E_{n_x,n_y,n_z} = \frac{\hbar^2\pi^2}{2m} \left[ \left( \frac{n_x}{L_x} \right)^2 + \left( \frac{n_y}{L_y} \right)^2 + \left( \frac{n_z}{L_z} \right)^2 \right] \quad (23)

with

:n_i=1,2,3,\ldots

Other

Molecules