Excess Gibbs Free Energy using Margules Two-Parameter Equation Solution

STEP 0: Pre-Calculation Summary
Formula Used
Excess Gibbs Free Energy = ([R]*Temperature*Mole Fraction of Component 1 in Liquid Phase*Mole Fraction of Component 2 in Liquid Phase)*(Margules Two Parameter Equation Coefficient (A21)*Mole Fraction of Component 1 in Liquid Phase+Margules Two Parameter Equation Coefficient (A12)*Mole Fraction of Component 2 in Liquid Phase)
GE = ([R]*Tactivity coefficent*x1*x2)*(A21*x1+A12*x2)
This formula uses 1 Constants, 6 Variables
Constants Used
[R] - Universal gas constant Value Taken As 8.31446261815324
Variables Used
Excess Gibbs Free Energy - (Measured in Joule) - Excess Gibbs Free Energy is the Gibbs energy of a solution in excess of what it would be if it were ideal.
Temperature - (Measured in Kelvin) - Temperature is the degree or intensity of heat present in a substance or object.
Mole Fraction of Component 1 in Liquid Phase - The mole fraction of component 1 in liquid phase can be defined as the ratio of the number of moles a component 1 to the total number of moles of components present in the liquid phase.
Mole Fraction of Component 2 in Liquid Phase - The mole fraction of component 2 in liquid phase can be defined as the ratio of the number of moles a component 2 to the total number of moles of components present in the liquid phase.
Margules Two Parameter Equation Coefficient (A21) - Margules two parameter equation coefficient (A21) is the coefficient used in Margules equation for the two-parameter model for component 2 the binary system.
Margules Two Parameter Equation Coefficient (A12) - Margules two parameter equation coefficient (A12) is the coefficient used in Margules equation for the two-parameter model for component 1 in the binary system.
STEP 1: Convert Input(s) to Base Unit
Temperature: 650 Kelvin --> 650 Kelvin No Conversion Required
Mole Fraction of Component 1 in Liquid Phase: 0.4 --> No Conversion Required
Mole Fraction of Component 2 in Liquid Phase: 0.6 --> No Conversion Required
Margules Two Parameter Equation Coefficient (A21): 0.58 --> No Conversion Required
Margules Two Parameter Equation Coefficient (A12): 0.56 --> No Conversion Required
STEP 2: Evaluate Formula
Substituting Input Values in Formula
GE = ([R]*Tactivity coefficent*x1*x2)*(A21*x1+A12*x2) --> ([R]*650*0.4*0.6)*(0.58*0.4+0.56*0.6)
Evaluating ... ...
GE = 736.727903669322
STEP 3: Convert Result to Output's Unit
736.727903669322 Joule --> No Conversion Required
FINAL ANSWER
736.727903669322 736.7279 Joule <-- Excess Gibbs Free Energy
(Calculation completed in 00.004 seconds)

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Correlations for Liquid Phase Activity Coefficients Calculators

Excess Gibbs Free Energy using Margules Two-Parameter Equation
​ LaTeX ​ Go Excess Gibbs Free Energy = ([R]*Temperature*Mole Fraction of Component 1 in Liquid Phase*Mole Fraction of Component 2 in Liquid Phase)*(Margules Two Parameter Equation Coefficient (A21)*Mole Fraction of Component 1 in Liquid Phase+Margules Two Parameter Equation Coefficient (A12)*Mole Fraction of Component 2 in Liquid Phase)
Activity Coefficient of Component 1 using Margules Two-Parameter Equation
​ LaTeX ​ Go Activity Coefficient of Component 1 = exp((Mole Fraction of Component 2 in Liquid Phase^2)*(Margules Two Parameter Equation Coefficient (A12)+2*(Margules Two Parameter Equation Coefficient (A21)-Margules Two Parameter Equation Coefficient (A12))*Mole Fraction of Component 1 in Liquid Phase))
Activity Coefficient of Component 1 using Margules One Parameter Equation
​ LaTeX ​ Go Activity Coefficient of Component 1 = exp(Margules One Parameter Equation Coefficient*(Mole Fraction of Component 2 in Liquid Phase^2))
Activity Coefficient of Component 2 using Margules One Parameter Equation
​ LaTeX ​ Go Activity Coefficient of Component 2 = exp(Margules One Parameter Equation Coefficient*(Mole Fraction of Component 1 in Liquid Phase^2))

Correlations for Liquid Phase Activity Coefficients Calculators

Activity Coefficient of Component 1 using Margules Two-Parameter Equation
​ LaTeX ​ Go Activity Coefficient of Component 1 = exp((Mole Fraction of Component 2 in Liquid Phase^2)*(Margules Two Parameter Equation Coefficient (A12)+2*(Margules Two Parameter Equation Coefficient (A21)-Margules Two Parameter Equation Coefficient (A12))*Mole Fraction of Component 1 in Liquid Phase))
Activity Coefficient of Component 1 using Van Laar Equation
​ LaTeX ​ Go Activity Coefficient of Component 1 = exp(Van Laar Equation Coefficient (A'12)*((1+((Van Laar Equation Coefficient (A'12)*Mole Fraction of Component 1 in Liquid Phase)/(Van Laar Equation Coefficient (A'21)*Mole Fraction of Component 2 in Liquid Phase)))^(-2)))
Activity Coefficient of Component 1 using Margules One Parameter Equation
​ LaTeX ​ Go Activity Coefficient of Component 1 = exp(Margules One Parameter Equation Coefficient*(Mole Fraction of Component 2 in Liquid Phase^2))
Activity Coefficient of Component 2 using Margules One Parameter Equation
​ LaTeX ​ Go Activity Coefficient of Component 2 = exp(Margules One Parameter Equation Coefficient*(Mole Fraction of Component 1 in Liquid Phase^2))

Excess Gibbs Free Energy using Margules Two-Parameter Equation Formula

​LaTeX ​Go
Excess Gibbs Free Energy = ([R]*Temperature*Mole Fraction of Component 1 in Liquid Phase*Mole Fraction of Component 2 in Liquid Phase)*(Margules Two Parameter Equation Coefficient (A21)*Mole Fraction of Component 1 in Liquid Phase+Margules Two Parameter Equation Coefficient (A12)*Mole Fraction of Component 2 in Liquid Phase)
GE = ([R]*Tactivity coefficent*x1*x2)*(A21*x1+A12*x2)

Give Information on Margules Activity Model.

The Margules activity model is a simple thermodynamic model for the excess Gibbs free energy of a liquid mixture introduced in 1895 by Max Margules. After Lewis had introduced the concept of the activity coefficient, the model could be used to derive an expression for the activity coefficients of a compound i in a liquid, a measure for the deviation from ideal solubility, also known as Raoult's law. In chemical engineering the Margules Gibbs free energy model for liquid mixtures is better known as the Margules activity or activity coefficient model. Although the model is old it has the characteristic feature to describe extrema in the activity coefficient, which modern models like NRTL and Wilson cannot.

What is Gibbs Free Energy?

The Gibbs free energy (or Gibbs energy) is a thermodynamic potential that can be used to calculate the maximum reversible work that may be performed by a thermodynamic system at a constant temperature and pressure. The Gibbs free energy measured in joules in SI) is the maximum amount of non-expansion work that can be extracted from a thermodynamically closed system (can exchange heat and work with its surroundings, but not matter). This maximum can be attained only in a completely reversible process. When a system transforms reversibly from an initial state to a final state, the decrease in Gibbs free energy equals the work done by the system to its surroundings, minus the work of the pressure forces.

How to Calculate Excess Gibbs Free Energy using Margules Two-Parameter Equation?

Excess Gibbs Free Energy using Margules Two-Parameter Equation calculator uses Excess Gibbs Free Energy = ([R]*Temperature*Mole Fraction of Component 1 in Liquid Phase*Mole Fraction of Component 2 in Liquid Phase)*(Margules Two Parameter Equation Coefficient (A21)*Mole Fraction of Component 1 in Liquid Phase+Margules Two Parameter Equation Coefficient (A12)*Mole Fraction of Component 2 in Liquid Phase) to calculate the Excess Gibbs Free Energy, The Excess Gibbs Free Energy using Margules Two-Parameter Equation formula is defined as the function of Margules two-parameter coefficients A12 and A21, temperature and the mole fraction of both the components 1 and 2. Excess Gibbs Free Energy is denoted by GE symbol.

How to calculate Excess Gibbs Free Energy using Margules Two-Parameter Equation using this online calculator? To use this online calculator for Excess Gibbs Free Energy using Margules Two-Parameter Equation, enter Temperature (Tactivity coefficent), Mole Fraction of Component 1 in Liquid Phase (x1), Mole Fraction of Component 2 in Liquid Phase (x2), Margules Two Parameter Equation Coefficient (A21) (A21) & Margules Two Parameter Equation Coefficient (A12) (A12) and hit the calculate button. Here is how the Excess Gibbs Free Energy using Margules Two-Parameter Equation calculation can be explained with given input values -> 736.7279 = ([R]*650*0.4*0.6)*(0.58*0.4+0.56*0.6).

FAQ

What is Excess Gibbs Free Energy using Margules Two-Parameter Equation?
The Excess Gibbs Free Energy using Margules Two-Parameter Equation formula is defined as the function of Margules two-parameter coefficients A12 and A21, temperature and the mole fraction of both the components 1 and 2 and is represented as GE = ([R]*Tactivity coefficent*x1*x2)*(A21*x1+A12*x2) or Excess Gibbs Free Energy = ([R]*Temperature*Mole Fraction of Component 1 in Liquid Phase*Mole Fraction of Component 2 in Liquid Phase)*(Margules Two Parameter Equation Coefficient (A21)*Mole Fraction of Component 1 in Liquid Phase+Margules Two Parameter Equation Coefficient (A12)*Mole Fraction of Component 2 in Liquid Phase). Temperature is the degree or intensity of heat present in a substance or object, The mole fraction of component 1 in liquid phase can be defined as the ratio of the number of moles a component 1 to the total number of moles of components present in the liquid phase, The mole fraction of component 2 in liquid phase can be defined as the ratio of the number of moles a component 2 to the total number of moles of components present in the liquid phase, Margules two parameter equation coefficient (A21) is the coefficient used in Margules equation for the two-parameter model for component 2 the binary system & Margules two parameter equation coefficient (A12) is the coefficient used in Margules equation for the two-parameter model for component 1 in the binary system.
How to calculate Excess Gibbs Free Energy using Margules Two-Parameter Equation?
The Excess Gibbs Free Energy using Margules Two-Parameter Equation formula is defined as the function of Margules two-parameter coefficients A12 and A21, temperature and the mole fraction of both the components 1 and 2 is calculated using Excess Gibbs Free Energy = ([R]*Temperature*Mole Fraction of Component 1 in Liquid Phase*Mole Fraction of Component 2 in Liquid Phase)*(Margules Two Parameter Equation Coefficient (A21)*Mole Fraction of Component 1 in Liquid Phase+Margules Two Parameter Equation Coefficient (A12)*Mole Fraction of Component 2 in Liquid Phase). To calculate Excess Gibbs Free Energy using Margules Two-Parameter Equation, you need Temperature (Tactivity coefficent), Mole Fraction of Component 1 in Liquid Phase (x1), Mole Fraction of Component 2 in Liquid Phase (x2), Margules Two Parameter Equation Coefficient (A21) (A21) & Margules Two Parameter Equation Coefficient (A12) (A12). With our tool, you need to enter the respective value for Temperature, Mole Fraction of Component 1 in Liquid Phase, Mole Fraction of Component 2 in Liquid Phase, Margules Two Parameter Equation Coefficient (A21) & Margules Two Parameter Equation Coefficient (A12) and hit the calculate button. You can also select the units (if any) for Input(s) and the Output as well.
How many ways are there to calculate Excess Gibbs Free Energy?
In this formula, Excess Gibbs Free Energy uses Temperature, Mole Fraction of Component 1 in Liquid Phase, Mole Fraction of Component 2 in Liquid Phase, Margules Two Parameter Equation Coefficient (A21) & Margules Two Parameter Equation Coefficient (A12). We can use 2 other way(s) to calculate the same, which is/are as follows -
  • Excess Gibbs Free Energy = ([R]*Temperature*Mole Fraction of Component 1 in Liquid Phase*Mole Fraction of Component 2 in Liquid Phase)*((Van Laar Equation Coefficient (A'12)*Van Laar Equation Coefficient (A'21))/(Van Laar Equation Coefficient (A'12)*Mole Fraction of Component 1 in Liquid Phase+Van Laar Equation Coefficient (A'21)*Mole Fraction of Component 2 in Liquid Phase))
  • Excess Gibbs Free Energy = ([R]*Temperature*Mole Fraction of Component 1 in Liquid Phase*Mole Fraction of Component 2 in Liquid Phase)*((Van Laar Equation Coefficient (A'12)*Van Laar Equation Coefficient (A'21))/(Van Laar Equation Coefficient (A'12)*Mole Fraction of Component 1 in Liquid Phase+Van Laar Equation Coefficient (A'21)*Mole Fraction of Component 2 in Liquid Phase))
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