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In a chemical process, chemical equilibrium is the state in which the chemical activities or concentrations of the reactants and products have no net change over time. Usually, this would be the state that results when the forward chemical process proceeds at the same rate as their reverse reaction. The reaction rates of the forward and reverse reactions are generally not zero but, being equal, there are no net changes in any of the reactant or product concentrations. This process is called dynamic equilibrium. ## Introduction

_{3}O^{+}} increases {CH_{3}CO_{2}H} must increase and {CH_{3}CO_{2}^{−}} must decrease._{c} varies with ionic strength, temperature and pressure (or volume). Likewise K_{p} for gases depends on partial pressure. These constants are easier to measure and encountered in high-school chemistry courses.
## Thermodynamics

### Treatment of activity

^{Software (below)}. However this is not always possible. It is common practice to assume that Γ is a constant, and to use the concentration quotient in place of the thermodynamic equilibrium constant. It is also general practice to use the term equilibrium constant instead of the more accurate concentration quotient. This practice will be followed here.### Justification for the use of concentration quotients

_{c} will vary with ionic strength. If it is measured at a series of different ionic strengths the value can be extrapolated to zero ionic strength. The concentration quotient obtained in this manner is known, paradoxically, as a thermodynamic equilibrium constant.### Metastable mixtures

## Pure compounds in equilibria

When pure substances (liquids or solids) are involved in equilibria they do not appear in the equilibrium equation ## Multiple equilibria

_{1} and K_{2} are examples of stepwise equilibrium constants. The overall equilibrium constant,$beta\_D$, is product of the stepwise constants.
_{1} and β_{2} are examples of association constants. Clearly β_{1} = 1/K_{2} and β_{2} = 1/β_{D}; lg β_{1} = pK_{2} and lg β_{2} = pK_{2} + pK_{1}
## Effect of temperature change on an equilibrium constant

## Types of equilibrium and some applications

## Composition of an equilibrium mixture

### Solving the equations of mass-balance

#### Composition for polybasic acids as a function of pH

The composition of solutions containing reactants A and H is easy to calculate as a function of p[H]. When [H] is known, the free concentration [A] is calculated from the mass-balance equation in A. Here is an example of the results that can be obtained.#### Solution equilibria with precipitation

The diagram above illustrates the point that a precipitate that is not one of the main species in the solution equilibrium may be formed. At pH just below 5.5 the main species present in a 5μM solution of Al^{3+} are aluminium hydroxides Al(OH)^{2+}, Al(OH)_{2}^{+} and Al_{13}(OH)_{32}^{7+}, but on raising the pH Al(OH)_{3} precipitates from the solution. This occurs because Al(OH)_{3} has a very large lattice energy. As the pH rises more and more Al(OH)_{3} comes out of solution. This is an example of Le Chatelier's principle in action: Increasing the concentration of the hydroxide ion causes more aluminium hydroxide to precipitate, which removes hydroxide from the solution. When the hydroxide concentration becomes sufficiently high the soluble aluminate, Al(OH)_{4}^{-}, is formed. ### Minimization of Gibbs energy

## See also

## References

## Further reading

## External links

### Computer programs for calculating species concentrations

There are n mass-balance equations in n unknown free concentrations. This constitutes a set of non-linear equations that must be solved by a method of successive approximations. The most commonly-used method is the Newton-Raphson method, which has been the subject of numerous publications. Some general computer programs are listed here.### Software for chemical equilibria

In a chemical reaction, when reactants are mixed together in a reaction vessel (and heated if needed), the whole of reactants do not get converted into the products. After some time (which may be shorter than millionths of a second or longer than the age of the universe), there will come a point when a fixed amount of reactants will exist in harmony with a fixed amount of products, the amounts of neither changing anymore. This is called chemical equilibrium.

The concept of chemical equilibrium was developed after Berthollet (1803) found that some chemical reactions are reversible. For any reaction such as

- $alpha\; A\; +\; beta\; B\; rightleftharpoons\; sigma\; S\; +\; tau\; T$

to be at equilibrium the rates of the forward and backward (reverse) reactions have to be equal. In this chemical equation with harpoon arrows pointing both ways to indicate equilibrium, A and B are reactant chemical species, S and T are product species, and α, β, σ, and τ are the stoichiometric coefficients of the respective reactants and products. The equilibrium position of a reaction is said to lie far to the right if, at equilibrium, nearly all the reactants are used up and far to the left if hardly any product is formed from the reactants.

Guldberg and Waage (1865), building on Berthollet’s ideas, proposed the law of mass action:

- $mbox\{forward\; reaction\; rate\}\; =\; k\_+\; \{A\}^alpha\{B\}^beta\; ,!$

- $mbox\{backward\; reaction\; rate\}\; =\; k\_\{-\}\; \{S\}^sigma\{T\}^tau\; ,!$

where A, B, S and T are active masses and k_{+} and k_{−} are rate constants. Since forward and backward rates are equal:

- $k\_+\; left\{\; A\; right\}^alpha\; left\{B\; right\}^beta\; =\; k\_\{-\}\; left\{S\; right\}^sigmaleft\{T\; right\}^tau\; ,$

and the ratio of the rate constants is also a constant, now known as an equilibrium constant.

- $K=frac\{k\_+\}\{k\_-\}=frac\{\{S\}^sigma\; \{T\}^tau\; \}\; \{\{A\}^alpha\; \{B\}^beta\}$

By convention the products form the numerator.
However, the law of mass action is valid only for concerted one-step reactions that proceed through a single transition state and is not valid in general because rate equations do not, in general, follow the stoichiometry of the reaction as Guldberg and Waage had proposed (see, for example, nucleophilic aliphatic substitution by S_{N}1 or reaction of hydrogen and bromine to form hydrogen bromide). Equality of forward and backward reaction rates, however, is a necessary condition for chemical equilibrium, though it is not sufficient to explain why equilibrium occurs.

Despite the failure of this derivation, the equilibrium constant for a reaction is indeed a constant, independent of the activities of the various species involved, though it does depend on temperature as observed by the van 't Hoff equation. Adding a catalyst will affect both the forward reaction and the reverse reaction in the same way and will not have an effect on the equilibrium constant. The catalyst will speed up both reactions thereby increasing the speed at which equilibrium is reached.

Although the macroscopic equilibrium concentrations are constant in time reactions do occur at the molecular level. For example, in the case of ethanoic acid dissolved in water and forming ethanoate and hydronium ions,

- CH
_{3}CO_{2}H + H_{2}O ⇌ CH_{3}CO_{2}^{−}+ H_{3}O^{+}

Le Chatelier's principle (1884) is a useful principle that gives a qualitative idea of an equilibrium system's response to changes in reaction conditions. If a dynamic equilibrium is disturbed by changing the conditions, the position of equilibrium moves to counteract the change. For example, adding more S from the outside will cause an excess of products, and the system will try to counteract this by increasing the reverse reaction and pushing the equilibrium point backward (though the equilibrium constant will stay the same).

If mineral acid is added to the ethanoic acid mixture, increasing the concentration of hydronium ion, the amount of dissociation must decrease as the reaction is driven to the left in accordance with this principle. This can also be deduced from the equilibrium constant expression for the reaction:

- $K=frac\{\{CH\_3CO\_2^-\}\{H\_3O^+\}\}\; \{\{CH\_3CO\_2H\}\{H\_2O\; \}\}$

A quantitative version is given by the reaction quotient.

J.W. Gibbs suggested in 1873 that equilibrium is attained when the Gibbs energy of the system is at its minimum value (assuming the reaction is carried out under constant pressure). What this means is that the derivative of the Gibbs energy with respect to reaction coordinate (a measure of the extent of reaction that has occurred, ranging from zero for all reactants to a maximum for all products) vanishes, signalling a stationary point. This derivative is usually called, for certain technical reasons, the Gibbs energy change. This criterion is both necessary and sufficient. If a mixture is not at equilibrium, the liberation of the excess Gibbs energy (or Helmholtz energy at constant volume reactions) is the “driving force” for the composition of the mixture to change until equilibrium is reached. The equilibrium constant can be related to the standard Gibbs energy change for the reaction by the equation

- $$

where R is the universal gas constant and T the temperature.

When the reactants are dissolved in a medium of high ionic strength the quotient of activity coefficients may be taken to be constant. In that case the concentration quotient, K_{c},

- $K\_c=frac\{[S]^sigma\; [T]^tau\; \}\; \{[A]^alpha\; [B]^beta\}$

The relationship between the Gibbs energy and the equilibrium constant can be found by considering chemical potentials. The thermodynamic condition for chemical equilibrium is

- At constant pressure ΔG=0 (ΔG is the change Gibbs free energy for the reaction)
- At constant volume ΔA=0 (ΔA is the change in Helmholtz free energy for the reaction)

In this article only the constant pressure case is considered. The constant volume case is important in geochemistry and atmospheric chemistry where pressure variations are significant. Note that, if reactants and products were in standard state (completely pure), then there would be no reversibility and no equilibrium. The mixing of the products and reactants contributes a large entropy (known as entropy of mixing) to states containing equal mixture of products and reactants. The combination of the standard Gibbs energy change and the Gibbs energy of mixing determines the equilibrium state.

In general an equilibrium system is defined by writing an equilibrium equation for the reaction

- $alpha\; A\; +\; beta\; B\; rightleftharpoons\; sigma\; S\; +\; tau\; T$

In order to meet the thermodynamic condition for equilibrium, the Gibbs energy must be stationary, meaning that the derivative of G with respect to reaction coordinate (ΔG) must be zero. It can be shown that ΔG is, in fact, equal to the difference between the chemical potentials of the products and those of the reactants. Therefore, the sum of the Gibbs energies of the reactants must be the equal to the sum of the Gibbs energies of the products.

- $alpha\; mu\_A\; +\; beta\; mu\_B\; =\; sigma\; mu\_S\; +\; tau\; mu\_T\; ,$

where μ is in this case a partial molar Gibbs energy, a chemical potential. The chemical potential of a reagent A is a function of the activity, {A} of that reagent.

- $mu\_A\; =\; mu\_\{A\}^\{ominus\}\; +\; RT\; ln\{A\}\; ,$

Substituting expressions like this into the Gibbs energy equation:

- $Delta\; G\; =\; Vdp-SdT+sum\_\{i=1\}^k\; mu\_i\; dN\_i\; +\; sum\_\{i=1\}^n\; X\_i\; da\_i\; +\; cdots\; ,$

which at constant pressure and temperature becomes:

- $Delta\; G\; =sum\_\{i=1\}^k\; mu\_i\; N\_i$

results in:

- $Delta\; G\; =\; sigma\; mu\_\{S\}\; +\; tau\; mu\_\{T\}\; -\; alpha\; mu\_\{A\}\; -\; beta\; mu\_\{B\}\; ,$

By substituting the chemical potentials:

- $Delta\; G\; =\; (sigma\; mu\_\{S\}^\{ominus\}\; +\; tau\; mu\_\{T\}^\{ominus\}\; )\; -\; (alpha\; mu\_\{A\}^\{ominus\}\; -\; beta\; mu\_\{B\}^\{ominus\}\; )\; +\; (sigma\; RT\; ln\{S\}\; +\; tau\; RT\; ln\{T\}\; )\; -\; (alpha\; RT\; ln\{A\}\; +\; beta\; RT\; ln\; \{B\}\; )$

the relationship becomes:

- $Delta\; G\; =sum\_\{i=1\}^k\; mu\_i^ominus\; v\_i\; +\; RT\; ln\; frac\{\{S\}^sigma\; \{T\}^tau\}\; \{\{A\}^alpha\; \{B\}^beta\}$

At equilibrium $Delta\; G\; =\; 0\; ,$ and therefore

- $sum\_\{i=1\}^k\; mu\_i^ominus\; v\_i\; +\; RT\; ln\; frac\{\{S\}^sigma\; \{T\}^tau\}\; \{\{A\}^alpha\; \{B\}^beta\}\; =\; 0$

leading to:

- $Delta\; G\_m^\{ominus\}\; =\; -RT\; ln\; K$

ΔG_{m}^{O} is the standard molar Gibbs energy change for the reaction and K is the equilibrium constant. Note that activities and equilibrium constants are dimensionless numbers.

The expression for the equilibrium constant can be re-written as the product of a concentration quotient, K_{c} and an activity coefficient quotient, Γ.

- $K=frac\{\{[S]\}\; ^sigma\; \{[T]\}^tau\; ...\; \}\; \{\{[A]\}^alpha\; \{[B]\}^beta\; ...\}$

For reactions in the gas phase partial pressure is used in place of concentration and fugacity coefficient in place of activity coefficient. In the real world, for example, when making ammonia in industry, fugacity coefficients must be taken into account. Fugacity, f, is the product of partial pressure and fugacity coefficient. The chemical potential of a species in the gas phase is given by

- $mu\; =\; mu^\{Theta\}\; +\; RT\; ln\; left(frac\{f\}\{bar\}\; right)\; +\; RT\; ln\; gamma$

In aqueous solution, equilibrium constants are usually determined in the presence of an "inert" electrolyte such as sodium nitrate NaNO_{3} or Potassium perchlorate KClO_{4}. The ionic strength, I, of a solution containing a dissolved salt, X^{+}Y^{-}, is given by

- $I\; =\; frac\{1\}\{2\}left(c\_X\; z\_X^2\; +\; c\_Y\; z\_Y^2\; +\; sum\_\{i=1\}^n\; c\_i\; z\_i^2right)$

- $K\_c\; =\; frac\{K\}\{Gamma\}$

To use a published value of an equilibrium constant in conditions of ionic strength different from the conditions used in its determination, the value should be adjusted^{Software (below)}.

A mixture may be appear to have no tendency to change, though it is not at equilibrium. For example, a mixture of SO_{2} and O_{2} is metastable as there is a kinetic barrier to formation of the product, SO_{3}.

- 2SO
_{2}+ O_{2}$rightleftharpoons$ 2SO_{3}

The barrier can be overcome when a catalyst is also present in the mixture as in the contact process, but the catalyst does not affect the equilibrium concentrations.

Likewise, the formation of bicarbonate from carbon dioxide and water is very slow under normal conditions

- CO
_{2}+ 2H_{2}O $rightleftharpoons$ HCO_{3}^{-}+H_{3}O^{+}

Applying the general formula for an equilibrium constant to the specific case of ethanoic acid one obtains

- $CH\_3CO\_2H\; +\; H\_2O\; rightleftharpoons\; CH\_3CO\_2^-\; +\; H\_3O^+$

- $K\_c=frac\{[\{CH\_3CO\_2\}^-][\{H\_3O\}^+]\}\; \{[\{CH\_3CO\_2H\}][\{H\_2O\}]\}$

- $K=frac\{[\{CH\_3CO\_2\}^-][\{H\_3O\}^+]\}\; \{[\{CH\_3CO\_2H\}]\}$

where now

$K=K\_c*[H\_2O],$

a constant factor is incorporated into the equilibrium constant.

A particular case is the self-ionization of water itself

- $H\_2O\; +\; H\_2O\; rightleftharpoons\; H\_3O^+\; +\; OH^-$

The self-ionization constant of water is defined as

$K\_w\; =\; [H^+][OH^-],$

It is perfectly legitimate to write [H^{+}] for the hydronium ion concentration, since the state of solvation of the proton is constant (in dilute solutions) and so does not affect the equilibrium concentrations. K_{w} varies with variation in ionic strength and/or temperature.

The concentrations of H^{+} and OH^{-} are not independent quantities. Most commonly [OH^{-}] is replaced by K_{w}[H^{+}]^{-1} in equilibrium constant expressions which would otherwise hydroxide.

Solids also do not appear in the equilibrium equation. An example is the Boudouard reaction :

- $2CO\; rightleftharpoons\; CO\_2\; +\; C$

for which the equation (without solid carbon) is written as:

- $K\_c=frac\{[CO\_2]\}\; \{[CO]^2\}$

Consider the case of a dibasic acid H_{2}A. When dissolved in water, the mixture will contain H_{2}A, HA^{-} and A^{2-}. This equilibrium can be split into two steps in each of which one proton is liberated.

- $H\_2A\; rightleftharpoons\; HA^-\; +\; H^+\; :K\_1=frac\{[HA^-][H^+]\}\; \{[H\_2A]\}$

- $HA^-\; rightleftharpoons\; A^\{2-\}\; +\; H^+\; :K\_2=frac\{[A^\{2-\}][H^+]\}\; \{[HA^-]\}$

- $H\_2A\; rightleftharpoons\; A^\{2-\}\; +\; 2H^+\; :beta\_D\; =\; frac\{[A^\{2-\}][H^+]^2\}\; \{[H\_2A]\}=K\_1K\_2$

- $A^\{2-\}\; +\; H^+\; rightleftharpoons\; HA^-\; :beta\_1=frac\; \{[HA^-]\}\; \{[A^\{2-\}][H^+]\}$

- $A^\{2-\}\; +\; 2H^+\; rightleftharpoons\; H\_2A\; :beta\_2=frac\; \{[H\_2A]\}\; \{[A^\{2-\}][H^+]^2\}$

The effect of changing temperature on an equilibrium constant is given by the van 't Hoff equation

- $frac\; \{dln\; K\}\; \{dT\}\; =\; frac\{\{Delta\; H\_m\}^\{Theta\}\}\; \{RT^2\}$

- $frac\; \{dln\; K\}\; \{d(1/T)\}\; =\; -frac\{\{Delta\; H\_m\}^\{Theta\}\}\; \{R\}$

- In the gas phase. Rocket engines
- The industrial synthesis such as ammonia in the Haber-Bosch process (depicted right) takes place through a succession of equilibrium steps including adsorbtion processes.
- atmospheric chemistry
- Seawater and other natural waters: Chemical oceanography
- Distribution between two phases
- LogD-Distribution coefficient: Important for pharmaceuticals where lipophilicity is a significant property of a drug
- Liquid-liquid extraction, Ion exchange, Chromatography
- Solubility product
- Uptake and release of oxygen by haemoglobin in blood
- Acid/base equilibria: Acid dissociation constant, hydrolysis, buffer solutions, indicators, acid-base homeostasis
- Metal-ligand complexation: sequestering agents, chelation therapy, MRI contrast reagents, Schlenk equilibrium
- Adduct formation: Host-guest chemistry, supramolecular chemistry, molecular recognition, dinitrogen tetroxide
- In certain oscillating reactions, the approach to equilibrium is not asymptotically but in the form of a damped oscillation .
- The related Nernst equation in electrochemistry gives the difference in electrode potential as a function of redox concentrations.
- When molecules on each side of the equilibrium are able to further react irreversibly in secondary reactions, the final product ratio is determined according to the Curtin-Hammett principle.

In these applications, terms such as stability constant, formation constant, binding constant, affinity constant, association/dissociation constant are used. In biochemistry, it is common to give units for binding constants, which serve to define the concentration units used when the constant’s value was determined.

When the only equilibrium is that of the formation of a 1:1 adduct as the composition of a mixture, there are any number of ways that the composition of a mixture can be calculated. For example, see ICE table for a traditional method of calculating the pH of a solution of a weak acid.

There are three approaches to the general calculation of the composition of a mixture at equilibrium.

- The most basic approach is to manipulate the various equilibrium constants until the desired concentrations are expressed in terms of measured equilibrium constants (equivalent to measuring chemical potentials) and initial conditions.
- Minimize the Gibbs energy of the system.
- Satisfy the equation of mass balance. The equations of mass balance are simply statements that demonstrate that the total concentration of each reactant must be constant by the law of conservation of mass.

In general, the calculations are rather complicated. For instance, in the case of a dibasic acid, H_{2}A dissolved in water the two reactants can be specified as the conjugate base, A^{2-}, and the proton, H^{+}. The following equations of mass-balance could apply equally well to a base such as 1,2-diaminoethane, in which case the base itself is designated as the reactant A:

- $T\_A\; =\; [A]\; +\; [HA]\; +[H\_2A]\; ,$

- $T\_H\; =\; [H]\; +\; [HA]\; +\; 2[H\_2A]\; -\; [OH]\; ,$

With T_{A} the total concentration of species A. Note that it is customary to omit the ionic charges when writing and using these equations.

When the equilibrium constants are known and the total concentrations are specified there are two equations in two unknown "free concentrations" [A] and [H]. This follows from the fact that [HA]= β_{1}[A][H], [H_{2}A]= β_{2}[A][H]^{2} and [OH] = K_{w}[H]^{-1}

- $T\_A\; =\; [A]\; +\; beta\_1[A][H]\; +\; beta\_2[A][H]^2\; ,$

- $T\_H\; =\; [H]\; +\; beta\_1[A][H]\; +\; 2beta\_2[A][H]^2\; -\; K\_w[H]^\{-1\}\; ,$

so the concentrations of the "complexes" are calculated from the free concentrations and the equilibrium constants. General expressions applicable to all systems with two reagents, A and B would be

- $T\_A=[A]+sum\_i\{p\_i\; beta\_i[A]^\{p\_i\}[B]^\{q\_i\}\}$

- $T\_B=[B]+sum\_i\{q\_i\; beta\_i[A]^\{p\_i\}[B]^\{q\_i\}\}$

This diagram, for the hydrolysis of the aluminium Lewis acid Al^{3+}_{aq} shows the species concentrations for a 5×10^{-6}M solution of an aluminium salt as a function of pH. Each concentration is shown as a percentage of the total aluminium.

Another common instance where precipitation occurs is when a metal cation interacts with an anionic ligand to form an electrically-neutral complex. If the complex is hydrophopbic, it will precipitate out of water. This occurs with the nickel ion Ni^{2+} and dimethylglyoxime, (dmgH_{2}): in this case the lattice energy of the solid is not particularly large, but it greatly exceeds the energy of solvation of the molecule Ni(dmgH)_{2}.

At equilibrium, G is at a minimum:

- $dG=\; sum\_\{j=1\}^m\; mu\_j,dN\_j\; =\; 0$

For a closed system, no particles may enter or leave, although they may combine in various ways. The total number of atoms of each element will remain constant. This means that the minimization above must be subjected to the constraints:

- $sum\_\{j=1\}^m\; a\_\{ij\}N\_j=b\_i^0$

where $a\_\{ij\}$ is the number of atoms of element i in molecule j and b_{i}^{0} is the total number of atoms of element i, which is a constant, since the system is closed. If there are a total of k types of atoms in the system, then there will be k such equations.

This is a standard problem in optimisation, known as constrained minimisation. The most common method of solving it is using the method of Lagrange multipliers, also known as undetermined multipliers (though other methods may be used).

Define:

- $mathcal\{G\}=\; G\; +\; sum\_\{i=1\}^klambda\_ileft(sum\_\{j=1\}^m\; a\_\{ij\}N\_j-b\_i^0right)=0$

where the $lambda\_i$ are the Lagrange multipliers, one for each element. This allows each of the $N\_j$ to be treated independently, and it can be shown using the tools of multivariate calculus that the equilibrium condition is given by

- $frac\{partial\; mathcal\{G\}\}\{partial\; N\_j\}=0$ and $frac\{partial\; mathcal\{G\}\}\{partial\; lambda\_i\}=0$

(For proof see Lagrange multipliers)

This is a set of (m+k) equations in (m+k) unknowns (the $N\_j$ and the $lambda\_i$) and may, therefore, be solved for the equilibrium concentrations $N\_j$ as long as the chemical potentials are known as functions of the concentrations at the given temperature and pressure. (See Thermodynamic databases for pure substances).

This method of calculating equilibrium chemical concentrations is useful for systems with a large number of different molecules. The use of k atomic element conservation equations for the mass constraint is straightforward, and replaces the use of the stoichiometric coefficient equations.

- Equilibrium constant
- Determination of equilibrium constants
- Henderson-Hasselbalch equation
- Michaelis-Menten kinetics
- Redox equilibria
- Thermodynamic databases for pure substances
- Autocatalytic reactions and order creation

- F. Van Zeggeren and S.H. Storey, The Computation of Chemical Equilibria, Cambridge University Press, 1970. Mainly concerned with gas-phase equilibria.
- D. J. Leggett (editor), Computational Methods for the Determination of Formation Constants, Plenum Press, 1985.
- A.E. Martell and R.J. Motekaitis, The Determination and Use of Stability Constants, Wiley-VCH, 1992.
- P. Gans, Stability Constants: Determination and Uses, an interactive CD, Protonic Software (Leeds), 2004

- HySS Titration simulation and speciation calculations.
- EQS4WIN A powerful computer program originally developed for gas-phase equilibria but subsequently extended to general applications. Uses the Gibbs energy minimization approach.
- CHEMEQLA comprehensive computer program for the calculation of thermodynamic equilibrium concentrations of species in homogeneous and heterogeneous systems. Many geochemical applications.
- WinSGW A Windows version of the SOLGASWATER computer program.
- Visual MINTEQ A Windows version of MINTEQA2 (ver 4.0). MINTEQA2 is a chemical equilibrium model for the calculation of metal speciation, solubility equilibria etc. for natural waters.
- MINEQL+ A chemical equilibrium modeling system for aqueous systems. Handles a wide range of pH, redox, solubility and sorption scenarios.

- Aqua solution software A set of five computer programs for
- Specific Interaction Theory. An editable database of published SIT parameters. Estimation of SIT parameters and adjustment of stability constants for changes in ionic strength.
- Calculation of electrolyte activity coefficients, ionic activity coefficients, osmotic coefficients
- Calculation of acid-base equilibria in electrolyte solutions and sea water
- Calculation of O
_{2}solubility in water, electrolyte solutions, natural fluids, and seawater as a function of temperature, concentration, salinity, altitude, external pressure, humidity - Prediction of temperature dependence of lg K values using various thermodynamic models
- JESS:A powerful research tool for thermodynamic and kinetic modelling of chemical speciation in complex aqueous environments.
- Chemical Equilibrium Calculator

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Last updated on Saturday October 04, 2008 at 09:02:39 PDT (GMT -0700)

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