Calculators Created by Shivam Sinha

Created Activity of Hydrogen Ion given pH

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Created Concentration of Hydrogen Ion given pH

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Created Concentration of Hydroxyl Ion given pOH

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Created Dissociation Constant of Weak Acid given pKa

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Created Dissociation Constant of Weak Base given pKb

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Created pH given Activity of Hydrogen Ion

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Created pH given Concentration of Hydrogen Ion

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Created pH of Mixture of Strong Acid and Strong Base when Solution is Acidic in Nature

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Created pH of Mixture of Two Strong Acids

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Created pKa given Dissociation Constant of Weak Acid

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Created pKb given Dissociation constant of Weak Base

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Created pOH given Concentration of Hydroxyl Ion

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Created pOH of Mixture of Strong Acid and Strong Base when Solution is Basic in Nature

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Created pOH of Mixture of Two Strong Bases

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Created Pressure using Saturated Temperature in Antoine Equation

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Created Saturated Pressure using Antoine Equation

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Created Saturated Temperature using Antoine Equation

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Created Temperature using Saturated Pressure in Antoine equation

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2 More Antoine Equation Calculators

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Created Actual Change in Enthalpy using Turbine Efficiency and Isentropic Change in Enthalpy

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Created Actual Enthalpy Change using Isentropic Compression Efficieny

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Created Actual Work done using Compressor Efficiency and Isentropic Shaft Work

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Created Actual Work Done using Turbine Efficiency and Isentropic Shaft Work

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Created Change in Enthalpy in Turbine (Expanders)

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Created Compressor Efficiency using Actual and Isentropic Change in Enthalpy

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Created Compressor Efficiency using Actual and Isentropic Shaft Work

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Created Enthalpy for Pumps using Volume Expansivity for Pump

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Created Entropy for Pumps using Volume Expansivity for Pump

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Created Isentropic Change in Enthalpy using Compressor Efficiency and Actual Change in Enthalpy

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Created Isentropic Change in Enthalpy using Turbine Efficiency and Actual Change in Enthalpy

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Created Isentropic Work done rate for Adiabatic Compression Process using Cp

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Created Isentropic Work Done Rate for Adiabatic Compression Process using Gamma

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Created Isentropic Work Done using Compressor Efficiency and Actual Shaft Work

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Created Isentropic Work Done using Turbine Efficiency and Actual Shaft Work

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Created Mass Flow Rate of Stream in Turbine (Expanders)

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Created Turbine Efficiency using Actual and Isentropic Shaft Work

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Created Volume Expansivity for Pumps using Enthalpy

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Created Volume Expansivity for Pumps using Entropy

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Created Work Done Rate by Turbine (Expanders)

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3 More Application of Thermodynamics to Flow Processes Calculators

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Created Liquid phase mole fraction using Gamma - phi formulation of VLE

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15 More Basic Formulas of Thermodynamics Calculators

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Created Concentration of Acid in Acidic Buffer using Henderson's Equation

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Created Concentration of Base in Basic Buffer using Henderson's Equation

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Created Concentration of Salt in Acidic Buffer using Henderson's equation

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Created Concentration of Salt in Basic Buffer using Henderson's Equation

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Created pH of Acidic Buffer using Henderson's Equation

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Created pKa of Acidic Buffer using Henderson's Equation

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Created pKb of Basic Buffer using Henderson's Equation

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Created pOH of Basic Buffer using Henderson's Equation

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3 More Buffer Solution Calculators

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Created pKa of Salt of Weak acid and Strong base

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Created pKb of Salt of Strong Acid and Weak base

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11 More Cationic and Anionic Salt Hydrolysis Calculators

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Created Molarity given Acidity and Normality

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Created Molarity given basicity and normality

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Created Molarity given Molality of Solution

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Created Molarity given Normality and Equivalent Mass

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Created Molarity given Normality and Number of Equivalents

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Created Molarity using Normality and Valency Factor

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Created Mole Fraction of Component 1 in Binary Solution

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Created Mole Fraction of Solute given Molarity

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Created Mole Fraction of Solvent given Molality

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13 More Concentration Terms Calculators

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Created Activity Coefficient of Component 1 using Margules One Parameter Equation

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Created Activity Coefficient of Component 1 using Margules Two-Parameter Equation

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Created Activity Coefficient of Component 1 using Van Laar Equation

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Created Activity Coefficient of Component 2 using Margules One Parameter Equation

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Created Activity Coefficient of Component 2 using Margules Two-Parameter Equation

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Created Activity Coefficient of Component 2 using Van Laar Equation

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Created Excess Gibbs Free Energy using Margules Two-Parameter Equation

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Created Excess Gibbs Free Energy using Van Laar Equation

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Verified Degree of Dissociation given Initial Vapor Density

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Verified Degree of Dissociation given Number of Moles at Equilibrium

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Verified Degree of Dissociation using Initial Vapour Density and Vapour Density at Equilibrium

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Verified Degree of Dissociation using Total Moles at Equilibrium

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4 More Degree of Dissociation Calculators

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Created Density of Solution given Molarity and Molality

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Created Density of Solution using Molarity of Solution

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15 More Density for Gases Calculators

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Verified Boiling point of Solvent given Ebullioscopic Constant and Latent Heat of Vaporization

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Verified Boiling point of Solvent given Ebullioscopic Constant and Molar Enthalpy of Vaporization

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Verified Molar Enthalpy of Vaporization given Boiling Point of Solvent

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Verified Molar Mass of Solvent given Ebullioscopic Constant

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20 More Elevation in Boiling Point Calculators

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Created Acentric Factor using B(0) and B(1) of Pitzer Correlations for Second Virial Coefficient

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Created Acentric Factor using Pitzer Correlations for Compressibility Factor

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Created Acentric Factor using Saturated Reduced Pressure given at Reduced Temperature 0.7

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Created B(0) given Z(0) using Pitzer Correlations for Second Virial Coefficient

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Created B(0) using Abbott Equations

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Created B(1) given Z(1) using Pitzer Correlations for Second Virial Coefficient

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Created B(1) using Abbott Equations

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Created Compressibility Factor using B(0) and B(1) of Pitzer Correlations for Second Virial Coefficient

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Created Compressibility Factor using Pitzer Correlations for Compressibility Factor

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Created Compressibility Factor using Reduced Second Virial Coefficient

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Created Compressibility Factor using Second Virial Coefficient

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Created Reduced Second Virial Coefficient using B(0) and B(1)

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Created Reduced Second Virial Coefficient using Compressibility Factor

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Created Reduced Second Virial Coefficient using Second Virial Coefficient

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Created Saturated Reduced Pressure at Reduced Temperature 0.7 using Acentric Factor

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Created Second Virial Coefficient using Compressibility Factor

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Created Second Virial Coefficient using Reduced Second Virial Coefficient

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Created Z(0) given B(0) using Pitzer Correlations for Second Virial Coefficient

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Created Z(1) given B(1) using Pitzer Correlations for Second Virial Coefficient

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2 More Equation of States Calculators

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Created Acidity given Equivalent Weight

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Created Basicity given Equivalent Weight

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Created Equivalent Weight for Acids

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Created Equivalent weight for base

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Created Equivalent Weight of Oxidising Agent

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Created Equivalent Weight of Reducing Agent

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Created Number of Electrons in Valence Shell

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Created Number of Electrons Left after Bonding

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Created Number of Moles of Electron Gained using Equivalent Weight of Oxidizing Agent

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Created Number of Moles of Electron Lost using Equivalent Weight of Reducing Agent

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Created Oxidation Number

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Created Valency Factor given Equivalent Weight

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3 More Equivalent Weight Calculators

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Created Actual Enthalpy using Excess and Ideal Solution Enthalpy

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Created Actual Entropy using Excess and Ideal Solution Entropy

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Created Actual Gibbs Energy using Excess and Ideal Solution Gibbs Energy

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Created Actual Volume using Excess and Ideal Solution Volume

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Created Excess Enthalpy using Actual and Ideal Solution Enthalpy

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Created Excess Entropy using Actual and Ideal Solution Entropy

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Created Excess Gibbs Energy using Actual and Ideal Solution Gibbs Energy

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Created Excess Volume using Actual and Ideal Solution Volume

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Created Ideal Solution Enthalpy using Excess and Actual Solution Enthalpy

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Created Ideal Solution Entropy using Excess and Actual Solution Entropy

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Created Ideal Solution Gibbs Energy using Excess and Actual Solution Gibbs Energy

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Created Ideal Solution Volume using Excess and Actual Solution Volume

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Verified Activation Energy for First Order Reaction

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Verified Arrhenius Constant for First Order Reaction

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Verified Rate Constant for First Order Reaction from Arrhenius Equation

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Verified Temperature in Arrhenius Equation for First Order Reaction

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14 More First Order Reaction Calculators

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Created Excess Gibbs Free Energy using Activity Coefficients and Liquid Mole Fractions

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Created Saturated Pressure of Comp. 1 using Second Virial Coefficient and Sat. Vapour Fugacity Coefficient

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Created Saturated Pressure of Comp. 2 using Second Virial Coefficient and Sat. Vapour Fugacity Coefficient

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Created Saturated Vapour Fugacity Coefficient of Comp. 1 using Sat. Pressure and Second Virial Coefficient

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Created Saturated Vapour Fugacity Coefficient of Comp. 2 using Sat. Pressure and Second Virial Coefficient

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Created Second Virial Coefficient of Comp. 1 using Sat. Pressure and Saturated Vapour Fugacity Coefficient

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Created Second Virial Coefficient of Comp. 2 using Saturated Pressure and Sat. Vapour Fugacity Coefficient

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Created Vapour Fugacity Coefficient of Comp. 1 using Sat. Pressure and Second Virial Coefficients

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Created Vapour Fugacity Coefficient of Comp. 2 using Sat. Pressure and Second Virial Coefficients

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Verified Adsorption Constant if n is equal to 1

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Verified Adsorption constant k using Freundlich Adsorption Constant

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Verified Mass of adsorbent if n is equal to 1

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Verified Mass of Adsorbent using Freundlich Adsorption Isotherm

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Verified Mass of Gas Adsorbed

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Verified Mass of gas adsorbed if n is equal to 1

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Verified Pressure of gas if n is equal to 1

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2 More Freundlich adsorption isotherm Calculators

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Created Fugacity of Liq. Phase Species using Poynting Factor

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Created Fugacity of Liq. Phase Species using Poynting Factor Correlation

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Created Poynting Factor using Saturated Fugacity Coeff. and Fugacity of Liq. Phase Species

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Created Saturated Fugacity Coeff. using Poynting Factor and Fugacity of Liq. Phase Species

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Created Saturated Fugacity Coeff. using Poynting Factor Correlation and Fugacity of Liq. Phase Species

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Created Saturated Pressure using Poynting Factor and Fugacity of Liq. Phase Species

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1 More Fugacity and Fugacity Coefficient Calculators

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Created Fugacity Coefficient using Gibbs Free Energy and Ideal Gibbs Free Energy

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Created Fugacity Coefficient using Residual Gibbs Free Energy

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Created Fugacity using Gibbs Free Energy, Ideal Gibbs Free Energy and Pressure

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Created Fugacity using Residual Gibbs Free Energy and Pressure

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Created Gibbs Free Energy using Ideal Gibbs Free Energy and Fugacity Coefficient

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Created Gibbs Free Energy using Ideal Gibbs Free Energy, Pressure and Fugacity

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Created Ideal Gibbs Free Energy using Gibbs Free Energy and Fugacity Coefficient

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Created Ideal Gibbs Free Energy using Gibbs Free Energy, Pressure and Fugacity Coefficient

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Created Pressure using Gibbs Free Energy, Ideal Gibbs Free Energy and Fugacity

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Created Pressure using Residual Gibbs Free Energy and Fugacity

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Created Residual Gibbs Free Energy using Fugacity and Pressure

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Created Residual Gibbs Free Energy using Fugacity Coefficient

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Created Temperature using Actual and Ideal Gibbs Free Energy and Fugacity Coefficient

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Created Temperature using Gibbs Free Energy, Ideal Gibbs Free Energy, Pressure and Fugacity

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Created Temperature using Residual Gibbs Free Energy and Fugacity

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Created Temperature using Residual Gibbs Free Energy and Fugacity Coefficient

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Created Constant of Hydrolysis given Ionic Product of Water and Acid Ionization Constant of Weak Acid

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Created Constant of Hydrolysis given Ionic Product of Water and Basic Ionization Constant of Weak Base

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Created Ionic Product of Water given Constant of Hydrolysis and Acid Ionization Constant of Weak Acid

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Created Ionic Product of Water given Constant of Hydrolysis and Basic Ionization Constant of Weak Base

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Created pKa of Salt of Weak Acid and Weak base

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Created pKb of Salt of Weak Acid and Weak base

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7 More Hydrolysis for Weak Acid and Weak Base Calculators

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Created Henry Law Constant using Mole Fraction and Partial Pressure of Gas

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Created Mole Fraction of Dissolved Gas using Henry Law

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Created Partial Pressure using Henry Law

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17 More Ideal Gas Calculators

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Created Ideal Gas Enthalpy using Ideal Gas Mixture Model in Binary System

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Created Ideal Gas Entropy using Ideal Gas Mixture Model in Binary System

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Created Ideal Gas Gibbs Free Energy using Ideal Gas Mixture Model in Binary System

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Created Ideal Gas Volume using Ideal Gas Mixture Model in Binary System

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Created Ideal Solution Enthalpy using Ideal Solution Model in Binary System

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Created Ideal Solution Entropy using Ideal Solution Model in Binary System

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Created Ideal Solution Gibbs Energy using Ideal Solution Model in Binary System

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Created Ideal Solution Volume using Ideal Solution Model in Binary System

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Created Activity Coefficient of Component using K-Value Expression for Gamma-Phi Formulation

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Created Activity Coefficient of Component using K-Value for Modified Raoult's Law

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Created Activity Coefficient using Gamma-Phi Formulation of VLE

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Created Fugacity Coefficient of Component using K-Value Expression for Gamma-Phi Formulation

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Created Fugacity Coefficient using Gamma-Phi Formulation of VLE

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Created K-Value of Component using Gamma-Phi Formulation

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Created K-Value of Component using Modified Raoult's Law

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Created K-Value of Component using Raoult's Law

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Created K-Value or Vapour-Liquid Distribution Ratio of Component

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Created Pressure of Component using K-Value Expression for Modified Raoult's Law

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Created Pressure using K-Value Expression for Gamma-Phi Formulation

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Created Pressure using K-value Expression for Raoult's Law

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Created Saturated Pressure of Component using K-value Expression for Gamma-Phi Formulation

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Created Saturated Pressure of Component using K-value Expression for Modified Raoult's Law

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Created Saturated Pressure of Component using K-value Expression for Raoult's Law

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Created Saturated Pressure using Gamma-Phi Formulation of VLE

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Created Total Pressure using Gamma-Phi Formulation of VLE

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Created Vapour Phase Mole Fraction using Gamma-Phi Formulation of VLE

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Verified Mass of Adsorbent for Langmuir Adsorption

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Verified Mass of Gas Adsorbed in grams for Langmuir Adsorption

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Verified Surface Area of Adsorbent Covered

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Verified Surface Area of Adsorbent Covered at Low Pressure

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1 More Langmuir Adsorption Isotherm Calculators

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Created Actual Work Produced by Utilizing Thermodynamic Efficiency and Conditions

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Created Actual Work using Ideal and Lost Work

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Created Actual Work using Thermodynamic Efficiency and Condition is Work is Required

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Created Heat using First Law of Thermodynamics

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Created Ideal Work using Lost and Actual Work

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Created Ideal Work using Thermodynamic Efficiency and Condition is Work is Produced

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Created Ideal Work using Thermodynamic Efficiency and Condition is Work is Required

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Created Internal Energy using First Law of Thermodynamics

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Created Lost Work using Ideal and Actual Work

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Created Rate of Actual Work using Rates of Ideal and Lost Work

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Created Rate of Ideal Work using Rates of Lost and Actual Work

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Created Rate of Lost Work using Rates of Ideal and Actual Work

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Created Thermodynamic Efficiency using Work Produced

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Created Thermodynamic Efficiency using Work Required

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Created Turbine Efficiency using Actual and Isentropic Change in Enthalpy

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Created Work using First Law of Thermodynamics

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Created Activity Coefficient for Component 1 for Infinite Dilution using NRTL Equation

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Created Activity Coefficient for Component 1 for Infinite Dilution using Wilson Equation

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Created Activity Coefficient for Component 1 using NRTL Equation

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Created Activity Coefficient for Component 1 using Wilson Equation

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Created Activity Coefficient for Component 2 for Infinite Dilution using NRTL Equation

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Created Activity Coefficient for Component 2 for Infinite Dilution using Wilson Equation

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Created Activity Coefficient for Component 2 using NRTL Equation

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Created Activity Coefficient for Component 2 using Wilson Equation

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Created Excess Gibbs Energy using Wilson Equation

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Created Excess Gibbs Free Energy using NRTL Equation

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Created Acidity given Molarity and Normality

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Created Basicity given Molarity and Normality

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Created Equivalent Mass given Molality and Normality

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Created Normality given Molality and Equivalent Mass

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Created Normality given Molarity and Acidity

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Created Normality given Molarity and Basicity

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Created Normality given Molarity and Number of Equivalents

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Created Normality given Molarity and Valency Factor

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Created Normality of substance 1 at Equivalence point

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Created Normality of substance 2 at Equivalence point

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Created Number of Equivalents given Molarity and Normality

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Created Number of Equivalents of Solute

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Created Number of Equivalents of Solute given Normality

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Created Number of Equivalents of Solute using Valency Factor

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Created Number of Moles of Solute given Number of Equivalents of Solute

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Created Valency Factor given Number of Equivalents of Solute

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Created Valency Factor using Molarity and Normality

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Created Volume of Solution given Normality

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Created Volume of Substance 1 at Equivalence Point

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Created Volume of substance 2 at equivalence point

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3 More Number of Equivalents and Normality Calculators

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Created Concentration of Anion given Ka and Concentration of Weak Acid and Hydrogen ion

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Created Concentration of Cation given Kb and Concentration of Weak Base and Hydroxyl ion

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Created Concentration of Hydrogen ion given Ka and Concentration of Weak Acid and Anion

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Created Concentration of Hydroxyl ion given Kb and Concentration of Weak Base and Cation

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Created Concentration of Weak Acid given Dissociation Constant and Concentration of Ions

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Created Concentration of Weak Base given Dissociation Constant and Concentration of Ions

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Created Degree of Dissociation given Ka and Initial Concentration

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Created Degree of Dissociation given Ka and Molar Volume of Weak Acid

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Created Degree of Dissociation given Kb and Initial Concentration

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Created Degree of Dissociation given Kb and Molar Volume of Weak Base

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Created Dissociation Constant Ka given Initial Concentration

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Created Dissociation Constant Ka given Initial Concentration of Weak Acid and Degree of Dissociation

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Created Dissociation Constant Kb given Initial Concentration

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Created Dissociation Constant Kb given Initial Concentration of Weak Base and Degree of Dissociation

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Created Dissociation constant of Weak Acid Ka given Concentration of Weak Acid and its Ions

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Created Dissociation constant of weak base Kb given concentration of weak base and its ions

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Created Initial Concentration of Weak Acid given Dissociation Constant Ka

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Created Initial Concentration of Weak Acid given Dissociation Constant Ka and Degree of Dissociation

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Created Initial Concentration of Weak Base given Dissociation Constant Kb

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Created Initial Concentration of Weak Base given Dissociation Constant Kb and Degree of Dissociation

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Created Mass of Solute using Mass Percent

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Created Mass of solute using Mass volume percent

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Created Mass of Solution given Mass Percent

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Created Mass Percent

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Created Mass Volume percent

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Created Volume of Solute using Volume Percent

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Created Volume of solution using Mass volume percent

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Created Volume of Solution using Volume Percent

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Created Volume Percent

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2 More Percentage Concentration Terms Calculators

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Created Activity Coefficient using Modified Raoult's Law in VLE

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Created Henry Law Constant using Henry Law in VLE

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Created Liquid Phase Mole Fraction using Henry Law in VLE

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Created Liquid Phase Mole Fraction using Modified Raoult's Law in VLE

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Created Liquid Phase Mole Fraction using Raoult's Law in VLE

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Created Poynting Factor

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Created Saturated Pressure using Modified Raoult's Law in VLE

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Created Saturated Pressure using Raoult's Law in VLE

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Created Total Pressure for Binary Liquid System for Dew-Bubble Point Calculations with Modified Raoult's Law

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Created Total Pressure for Binary Liquid System for Dew-Bubble Point Calculations with Raoult's Law

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Created Total Pressure for Binary Vapour System for Dew-Bubble Point calculations with Modified Raoult's Law

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Created Total Pressure for Binary Vapour System for Dew-Bubble Point Calculations with Raoult's Law

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Created Total Pressure using Henry Law in VLE

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Created Total Pressure using Modified Raoult's Law in VLE

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Created Total Pressure using Raoult's Law in VLE

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Created Vapour Phase Mole Fraction using Henry Law in VLE

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Created Vapour Phase Mole Fraction using Modified Raoult's Law in VLE

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Created Vapour Phase Mole Fraction using Raoult's Law in VLE

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Verified Equilibrium Constant due to Pressure given Degree of Dissociation

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19 More Relation between Equilibrium Constant and Degree of Dissociation Calculators

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Verified Initial Total Moles using Degree of Dissociation

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Verified Initial Vapour Density given Degree of Dissociation

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Verified Number of moles of products using degree of dissociation

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Verified Number of Moles of Substance A and B at Equilibrium

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Verified Total Moles at Equilibrium using Degree of Dissociation

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19 More Relation between Vapour Density and Degree of Dissociation Calculators

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Created Concentration of Acid 1 given Relative Strength, Conc of Acid 2 and Degree of Diss of both Acids

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Created Concentration of Acid 1 given Relative Strength, Conc of Acid 2 and Diss const of both Acids

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Created Concentration of Acid 2 given Relative Strength, Conc of Acid 1 and Degree of Diss of both Acids

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Created Concentration of Acid 2 given Relative Strength, Conc of Acid 1 and Diss Const of both Acids

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Created Concentration of Hydrogen Ion of Acid 1 given Relative Strength and Conc of Hydrogen Ion of Acid 2

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Created Concentration of Hydrogen Ion of Acid 2 given Relative Strength and Conc of Hydrogen Ion of Acid 1

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Created Degree of Dissociation 1 given Relative Strength, Conc of both Acid and Degree of Diss 2

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Created Degree of Dissociation 2 given Relative Strength, Conc of both Acid and Degree of Diss 1

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Created Dissociation Constant 1 given Relative Strength, Conc of both Acid and Diss Const 2

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Created Dissociation Constant 2 given Relative Strength, Conc of both Acid and Diss Const 1

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Created Relative Strength of Two Acids given Concentration and Degree of Dissociations of both Acids

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Created Relative Strength of Two Acids given Concentration and Dissociation Constant of both Acids

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Created Relative Strength of Two Acids given Concentration of Hydrogen Ion of both Acids

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Created Actual Enthalpy using Residual and Ideal Gas Enthalpy

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Created Actual Entropy using Residual and Ideal Gas Entropy

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Created Actual Gibbs Energy using Residual and Ideal Gas Gibbs Energy

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Created Actual Volume using Residual and Ideal Gas Volume

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Created Ideal Gas Enthalpy using Residual and Actual Gas Enthalpy

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Created Ideal Gas Entropy using Residual and Actual Gas Entropy

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Created Ideal Gas Gibbs Free Energy using Residual and Actual Gas Gibbs Energy

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Created Ideal Gas Volume using Residual and Actual Gas Volume

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Created Residual Enthalpy using Actual and Ideal Gas Enthalpy

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Created Residual Entropy using Actual and Ideal Gas Entropy

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Created Residual Gibbs Free Energy using Actual and Ideal Gas Gibbs Free Energy

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Created Residual Volume using Actual and Ideal Gas Volume

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Verified Activation Energy for Second Order Reaction

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Verified Arrhenius Constant for Second Order Reaction

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Verified Rate Constant for Second Order Reaction from Arrhenius Equation

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Verified Temperature in Arrhenius Equation for Second Order Reaction

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11 More Second Order Reaction Calculators

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Created Enthalpy using Gibbs Free Energy, Temperature and Entropy

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Created Enthalpy using Internal Energy, Pressure and Volume

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Created Entropy using Gibbs Free Energy, Enthalpy and Temperature

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Created Entropy using Helmholtz Free Energy, Internal Energy and Temperature

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Created Gibbs Free Energy using Enthalpy, Temperature and Entropy

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Created Helmholtz Free Energy using Internal Energy, Temperature and Entropy

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Created Internal Energy using Enthalpy, Pressure and Volume

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Created Internal Energy using Helmholtz Free Energy, Temperature and Entropy

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Created Pressure using Enthalpy, Internal Energy and Volume

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Created Temperature using Gibbs Free Energy, Enthalpy and Entropy

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Created Temperature using Helmholtz Free Energy, Internal Energy and Entropy

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Created Volume using Enthalpy, Internal Energy and Pressure

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Verified Equilibrium Constant due to Pressure Given Gibbs Energy

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Verified Gibbs Free Energy given Equilibrium Constant due to Pressure

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Verified Temperature of Reaction given Equilibrium Constant of Pressure and Gibbs Energy

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22 More Thermodynamics in Chemical Equilibrium Calculators

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Verified Vapour Density at Equilibrium using Degree of Dissociation

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8 More Vapour Density at Equilibrium Calculators

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Verified Energy of Vibrational Transitions

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14 More Vibrational Energy Levels Calculators

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Verified Anharmonicity Constant given First Overtone Frequency

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Verified Anharmonicity Constant given Second Overtone Frequency

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Verified First Overtone Frequency

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Verified Second Overtone Frequency

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Verified Vibrational Degree of Freedom for Linear Molecules

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Verified Vibrational Degree of Freedom for Nonlinear Molecules

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Verified Vibrational Frequency given First Overtone Frequency

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Verified Vibrational Frequency given Second Overtone Frequency

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14 More Vibrational Spectroscopy Calculators

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Verified Activation Energy for Zero Order Reactions

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Verified Arrhenius Constant for Zero Order Reaction

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Verified Rate Constant for Zero Order Reaction from Arrhenius Equation

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Verified Temperature in Arrhenius Equation for Zero Order Reaction

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15 More Zero Order Reaction Calculators

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List of Calculators by Shivam Sinha