Calculators Created by Shivam Sinha

Created Activity of Hydrogen Ion given pH

Go

Created Concentration of Hydrogen Ion given pH

Go

Created Concentration of Hydroxyl Ion given pOH

Go

Created Dissociation Constant of Weak Acid given pKa

Go

Created Dissociation Constant of Weak Base given pKb

Go

Created pH given Activity of Hydrogen Ion

Go

Created pH given Concentration of Hydrogen Ion

Go

Created pKa given Dissociation Constant of Weak Acid

Go

Created pKb given Dissociation constant of Weak Base

Go

Created pOH given Concentration of Hydroxyl Ion

Go

Created pKa of Salt of Weak acid and Strong base

Go

5 More Anionic Salt Hydrolysis Calculators

Go

Created Pressure using Saturated Temperature in Antoine Equation

Go

Created Saturated Pressure using Antoine Equation

Go

Created Saturated Temperature using Antoine Equation

Go

Created Temperature using Saturated Pressure in Antoine equation

Go

2 More Antoine Equation Calculators

Go

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

Go

Created Actual Enthalpy Change using Isentropic Compression Efficieny

Go

Created Actual Work done using Compressor Efficiency and Isentropic Shaft Work

Go

Created Actual Work Done Using Turbine Efficiency and Isentropic Shaft Work

Go

Created Change in Enthalpy in Turbine (Expanders)

Go

Created Compressor Efficiency Using Actual and Isentropic Change in Enthalpy

Go

Created Compressor Efficiency Using Actual and Isentropic Shaft Work

Go

Created Enthalpy for Pumps Using Volume Expansivity for Pump

Go

Created Entropy for Pumps Using Volume Expansivity for Pump

Go

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

Go

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

Go

Created Isentropic Work done rate for Adiabatic Compression Process Using Cp

Go

Created Isentropic Work Done Rate for Adiabatic Compression Process Using Gamma

Go

Created Isentropic Work Done Using Compressor Efficiency and Actual Shaft Work

Go

Created Isentropic Work Done Using Turbine Efficiency and Actual Shaft Work

Go

Created Mass Flow Rate of Stream in Turbine (Expanders)

Go

Created Turbine Efficiency Using Actual and Isentropic Shaft Work

Go

Created Volume Expansivity for Pumps Using Enthalpy

Go

Created Volume Expansivity for Pumps Using Entropy

Go

Created Work Done Rate by Turbine (Expanders)

Go

3 More Application of Thermodynamics to Flow Processes Calculators

Go

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

Go

15 More Basic Formulas of Thermodynamics Calculators

Go

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

Go

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

Go

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

Go

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

Go

Created pH of Acidic Buffer using Henderson's Equation

Go

Created pKa of Acidic Buffer using Henderson's Equation

Go

Created pKb of Basic Buffer using Henderson's Equation

Go

Created pOH of Basic Buffer using Henderson's Equation

Go

3 More Buffer Solution Calculators

Go

Created pKb of Salt of Strong Acid and Weak base

Go

6 More Cationic Salt Hydrolysis Calculators

Go

Verified Rate Constant for First Order Reaction from Arrhenius Equation

Go

Verified Rate Constant for Zero Order Reaction from Arrhenius Equation

Go

6 More Chemical Kinetics Calculators

Go

Created Molarity given Acidity and Normality

Go

Created Molarity given basicity and normality

Go

Created Molarity given Molality of Solution

Go

Created Molarity given Normality and Equivalent Mass

Go

Created Molarity given Normality and Number of Equivalents

Go

Created Molarity using Normality and Valency Factor

Go

Created Mole Fraction of Component 1 in Binary Solution

Go

Created Mole Fraction of Solute given Molarity

Go

Created Mole Fraction of Solvent given Molality

Go

13 More Concentration Terms Calculators

Go

Created Activity Coefficient of Component 1 using Margules One Parameter Equation

Go

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

Go

Created Activity Coefficient of Component 1 using Van Laar Equation

Go

Created Activity Coefficient of Component 2 using Margules One Parameter Equation

Go

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

Go

Created Activity Coefficient of Component 2 using Van Laar Equation

Go

Created Excess Gibbs Free Energy using Margules Two-Parameter Equation

Go

Created Excess Gibbs Free Energy using Van Laar Equation

Go

Verified Degree of Dissociation given Initial Vapor Density

Go

Verified Degree of Dissociation given Number of Moles at Equilibrium

Go

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

Go

Verified Degree of Dissociation Using Total Moles at Equilibrium

Go

4 More Degree of Dissociation Calculators

Go

Created Density of Solution given Molarity and Molality

Go

Created Density of Solution using Molarity of Solution

Go

15 More Density for gases Calculators

Go

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

Go

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

Go

Verified Molar Enthalpy of Vaporization given Boiling point of solvent

Go

Verified Molar Mass of solvent given Ebullioscopic Constant

Go

13 More Elevation in Boiling Point Calculators

Go

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

Go

Created Acentric Factor using Pitzer Correlations for Compressibility Factor

Go

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

Go

Created B(0) using Abbott Equations

Go

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

Go

Created B(1) using Abbott Equations

Go

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

Go

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

Go

Created Compressibility Factor using Pitzer Correlations for Compressibility Factor

Go

Created Compressibility Factor using Reduced Second Virial Coefficient

Go

Created Compressibility Factor using Second Virial Coefficient

Go

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

Go

Created Reduced Second Virial Coefficient using Compressibility Factor

Go

Created Reduced Second Virial Coefficient using Second Virial Coefficient

Go

Created Saturated Reduced Pressure at Reduced Temperature 0.7 using Acentric Factor

Go

Created Second Virial Coefficient using Compressibility Factor

Go

Created Second Virial Coefficient using Reduced Second Virial Coefficient

Go

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

Go

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

Go

2 More Equation of States Calculators

Go

Created Acidity given Equivalent Weight

Go

Created Basicity given Equivalent Weight

Go

Created Equivalent Weight for Acids

Go

Created Equivalent weight for base

Go

Created Equivalent Weight of Oxidising Agent

Go

Created Equivalent Weight of Reducing Agent

Go

Created Number of Electrons in Valence Shell

Go

Created Number of Electrons Left after Bonding

Go

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

Go

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

Go

Created Oxidation Number

Go

Created Valency Factor given Equivalent Weight

Go

3 More Equivalent weight Calculators

Go

Created Actual Enthalpy using Excess and Ideal Solution Enthalpy

Go

Created Actual Entropy using Excess and Ideal Solution Entropy

Go

Created Actual Gibbs Energy using Excess and Ideal Solution Gibbs Energy

Go

Created Actual Volume using Excess and Ideal Solution Volume

Go

Created Excess Enthalpy using Actual and Ideal Solution Enthalpy

Go

Created Excess Entropy using Actual and Ideal Solution Entropy

Go

Created Excess Gibbs Energy using Actual and Ideal Solution Gibbs Energy

Go

Created Excess Volume using Actual and Ideal Solution Volume

Go

Created Ideal Solution Enthalpy using Excess and Actual Solution Enthalpy

Go

Created Ideal Solution Entropy using Excess and Actual Solution Entropy

Go

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

Go

Created Ideal Solution Volume using Excess and Actual Solution Volume

Go

Verified Activation energy for first order reaction

Go

Verified Arrhenius Constant for First Order Reaction

Go

Verified Temperature in Arrhenius Equation for First Order Reaction

Go

13 More First Order Reaction Calculators

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

Verified Adsorption Constant if n is equal to 1

Go

Verified Adsorption constant k using Freundlich adsorption constant

Go

Verified Mass of adsorbent if n is equal to 1

Go

Verified Mass of adsorbent using Freundlich adsorption isotherm

Go

Verified Mass of gas adsorbed

Go

Verified Mass of gas adsorbed if n is equal to 1

Go

Verified Pressure of gas if n is equal to 1

Go

2 More Freundlich adsorption isotherm Calculators

Go

Created Fugacity of Liq. Phase Species using Poynting Factor

Go

Created Fugacity of Liq. Phase Species using Poynting Factor Correlation

Go

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

Go

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

Go

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

Go

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

Go

1 More Fugacity and Fugacity Coefficient Calculators

Go

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

Go

Created Fugacity Coefficient using Residual Gibbs Free Energy

Go

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

Go

Created Fugacity using Residual Gibbs Free Energy and Pressure

Go

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

Go

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

Go

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

Go

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

Go

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

Go

Created Pressure using Residual Gibbs Free Energy and Fugacity

Go

Created Residual Gibbs Free Energy using Fugacity and Pressure

Go

Created Residual Gibbs Free Energy using Fugacity Coefficient

Go

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

Go

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

Go

Created Temperature using Residual Gibbs Free Energy and Fugacity

Go

Created Temperature using Residual Gibbs Free Energy and Fugacity Coefficient

Go

Created pKa of Salt of Weak Acid and Weak base

Go

Created pKb of Salt of Weak Acid and Weak base

Go

5 More Hydrolysis for Weak Acid and Weak Base Calculators

Go

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

Go

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

Go

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

Go

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

Go

2 More Hydrolysis of Cations or Anions Calculators

Go

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

Go

Created Mole Fraction of Dissolved Gas using Henry Law

Go

Created Partial Pressure using Henry Law

Go

18 More Ideal Gas Calculators

Go

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

Go

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

Go

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

Go

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

Go

Created Ideal Solution Enthalpy using Ideal Solution Model in Binary System

Go

Created Ideal Solution Entropy using Ideal Solution Model in Binary System

Go

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

Go

Created Ideal Solution Volume using Ideal Solution Model in Binary System

Go

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

Go

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

Go

Created Activity Coefficient using Gamma-Phi Formulation of VLE

Go

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

Go

Created Fugacity Coefficient using Gamma-Phi Formulation of VLE

Go

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

Go

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

Go

Created K-Value of Component using Gamma-Phi Formulation

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

Created Saturated Pressure using Gamma-Phi Formulation of VLE

Go

Created Total Pressure using Gamma-Phi Formulation of VLE

Go

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

Go

Verified Mass of Adsorbent for Langmuir Adsorption

Go

Verified Mass of Gas Adsorbed in grams for Langmuir Adsorption

Go

Verified Surface Area of Adsorbent Covered

Go

Verified Surface Area of Adsorbent Covered at Low Pressure

Go

1 More Langmuir Adsorption Isotherm Calculators

Go

Created Actual Work using Ideal and Lost Work

Go

Created Actual Work using Thermodynamic Efficiency and the Condition is Work is Produced

Go

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

Go

Created Heat using The First Law of Thermodynamics

Go

Created Ideal Work using Lost and Actual Work

Go

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

Go

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

Go

Created Internal Energy using First Law of Thermodynamics

Go

Created Lost Work using Ideal and Actual Work

Go

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

Go

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

Go

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

Go

Created Thermodynamic Efficiency using Work Produced

Go

Created Thermodynamic Efficiency using Work Required

Go

Created Turbine Efficiency using Actual and Isentropic Change in Enthalpy

Go

Created Work using The First Law of Thermodynamics

Go

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

Go

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

Go

Created Activity Coefficient for Component 1 using NRTL Equation

Go

Created Activity Coefficient for Component 1 using Wilson Equation

Go

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

Go

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

Go

Created Activity Coefficient for Component 2 using NRTL Equation

Go

Created Activity Coefficient for Component 2 using Wilson Equation

Go

Created Excess Gibbs Energy using Wilson Equation

Go

Created Excess Gibbs Free Energy using NRTL Equation

Go

Created Acidity given molarity and normality

Go

Created Basicity given molarity and normality

Go

Created Equivalent mass given molality and normality

Go

Created Normality given molality and equivalent mass

Go

Created Normality given molarity and acidity

Go

Created Normality given molarity and basicity

Go

Created Normality given molarity and number of equivalents

Go

Created Normality given Molarity and Valency Factor

Go

Created Normality of substance 1 at equivalence point

Go

Created Normality of substance 2 at equivalence point

Go

Created Number of equivalents given molarity and normality

Go

Created Number of equivalents of solute

Go

Created Number of equivalents of solute given normality

Go

Created Number of Equivalents of Solute using Valency Factor

Go

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

Go

Created Valency Factor given Number of Equivalents of Solute

Go

Created Valency Factor using Molarity and Normality

Go

Created Volume of solution given normality

Go

Created Volume of substance 1 at equivalence point

Go

Created Volume of substance 2 at equivalence point

Go

2 More Number of equivalents and normality Calculators

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

Created Degree of Dissociation given Ka and Initial Concentration

Go

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

Go

Created Degree of Dissociation given Kb and Initial Concentration

Go

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

Go

Created Dissociation Constant Ka given Initial Concentration

Go

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

Go

Created Dissociation Constant Kb given Initial Concentration

Go

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

Go

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

Go

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

Go

Created Initial Concentration of Weak Acid given Dissociation Constant Ka

Go

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

Go

Created Initial Concentration of Weak Base given Dissociation Constant Kb

Go

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

Go

Created Mass of solute using mass percent

Go

Created Mass of solute using Mass volume percent

Go

Created Mass of solution using mass percent

Go

Created Mass Percent

Go

Created Mass Volume percent

Go

Created Volume of solute using volume percent

Go

Created Volume of solution using Mass volume percent

Go

Created Volume of solution using volume percent

Go

Created Volume percent

Go

2 More Percentage concentration terms Calculators

Go

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

Go

Created pH of Mixture of Two Strong Acids

Go

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

Go

Created pOH of Mixture of Two Strong Bases

Go

Created Activity Coefficient using Modified Raoult's Law in VLE

Go

Created Henry Law Constant using Henry Law in VLE

Go

Created Liquid Phase Mole Fraction using Henry Law in VLE

Go

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

Go

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

Go

Created Poynting Factor

Go

Created Saturated Pressure using Modified Raoult's Law in VLE

Go

Created Saturated Pressure using Raoult's Law in VLE

Go

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

Go

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

Go

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

Go

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

Go

Created Total Pressure using Henry Law in VLE

Go

Created Total Pressure using Modified Raoult's Law in VLE

Go

Created Total Pressure using Raoult's Law in VLE

Go

Created Vapour Phase Mole Fraction using Henry Law in VLE

Go

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

Go

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

Go

Verified Equilibrium Constant due to Pressure given Degree of Dissociation

Go

19 More Relation between equilibrium constant and degree of dissociation Calculators

Go

Verified Initial Total Moles using Degree of Dissociation

Go

Verified Initial Vapour Density given Degree of Dissociation

Go

Verified Number of moles of products using degree of dissociation

Go

Verified Number of Moles of Substance A and B at Equilibrium

Go

Verified Total Moles at Equilibrium using Degree of Dissociation

Go

19 More Relation between vapour density and degree of dissociation Calculators

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

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

Go

Created Relative Strength of two acids given concentration and dissociation constant of both acids

Go

Created Relative Strength of two acids given concentration of hydrogen ion of both acids

Go

Created Actual Enthalpy using Residual and Ideal Gas Enthalpy

Go

Created Actual Entropy using Residual and Ideal Gas Entropy

Go

Created Actual Gibbs Energy using Residual and Ideal Gas Gibbs Energy

Go

Created Actual Volume using Residual and Ideal Gas Volume

Go

Created Ideal Gas Enthalpy using Residual and Actual Gas Enthalpy

Go

Created Ideal Gas Entropy using Residual and Actual Gas Entropy

Go

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

Go

Created Ideal Gas Volume using Residual and Actual Gas Volume

Go

Created Residual Enthalpy using Actual and Ideal Gas Enthalpy

Go

Created Residual Entropy using Actual and Ideal Gas Entropy

Go

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

Go

Created Residual Volume using Actual and Ideal Gas Volume

Go

Verified Activation energy for second order reaction

Go

Verified Arrhenius Constant for Second Order Reaction

Go

Verified Rate Constant for Second Order Reaction from Arrhenius Equation

Go

Verified Temperature in Arrhenius Equation for Second Order Reaction

Go

8 More Second Order Reaction Calculators

Go

Created Enthalpy using Gibbs Free Energy, Temperature and Entropy

Go

Created Enthalpy using Internal Energy, Pressure and Volume

Go

Created Entropy using Gibbs Free Energy, Enthalpy and Temperature

Go

Created Entropy using Helmholtz Free Energy, Internal Energy and Temperature

Go

Created Gibbs Free Energy using Enthalpy, Temperature and Entropy

Go

Created Helmholtz Free Energy using Internal Energy, Temperature and Entropy

Go

Created Internal Energy using Enthalpy, Pressure and Volume

Go

Created Internal Energy using Helmholtz Free Energy, Temperature and Entropy

Go

Created Pressure using Enthalpy, Internal Energy and Volume

Go

Created Temperature using Gibbs Free Energy, Enthalpy and Entropy

Go

Created Temperature using Helmholtz Free Energy, Internal Energy and Entropy

Go

Created Volume using Enthalpy, Internal Energy and Pressure

Go

Verified Equilibrium Constant due to Pressure Given Gibbs Energy

Go

Verified Gibbs Free Energy given Equilibrium Constant due to Pressure

Go

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

Go

22 More Thermodynamics in chemical equilibrium Calculators

Go

Verified Vapour Density at Equilibrium using Degree of Dissociation

Go

8 More Vapour Density at Equilibrium Calculators

Go

Verified Energy of Vibrational Transitions

Go

14 More Vibrational Energy Levels Calculators

Go

Verified Anharmonicity Constant given First Overtone Frequency

Go

Verified Anharmonicity Constant given Second Overtone Frequency

Go

Verified First Overtone Frequency

Go

Verified Second Overtone Frequency

Go

Verified Vibrational Degree of Freedom for Linear Molecules

Go

Verified Vibrational Degree of Freedom for Nonlinear Molecules

Go

Verified Vibrational Frequency given First Overtone Frequency

Go

Verified Vibrational Frequency given Second Overtone Frequency

Go

13 More Vibrational spectroscopy Calculators

Go

Verified Activation Energy for Zero Order Reactions

Go

Verified Arrhenius Constant for Zero Order Reaction

Go

Verified Temperature in Arrhenius Equation for Zero Order Reaction

Go

15 More Zero Order Reaction Calculators

Go

List of Calculators by Shivam Sinha