Mole Fraction of Dissolved Gas using Henry Law Solution

STEP 0: Pre-Calculation Summary
Formula Used
Mole Fraction of Component in Liquid Phase = Partial Pressure/Henry Law Constant
xLiquid = ppartial/KH
This formula uses 3 Variables
Variables Used
Mole Fraction of Component in Liquid Phase - The Mole Fraction of Component in Liquid Phase can be defined as the ratio of the number of moles a component to the total number of moles of components present in the liquid phase.
Partial Pressure - (Measured in Pascal) - Partial Pressure is the notional pressure of that constituent gas if it alone occupied the entire volume of the original mixture at the same temperature.
Henry Law Constant - (Measured in Pascal Cubic Meter per Mole) - Henry Law Constant is a measure of the concentration of a chemical in air over its concentration in water.
STEP 1: Convert Input(s) to Base Unit
Partial Pressure: 0.2 Pascal --> 0.2 Pascal No Conversion Required
Henry Law Constant: 200000 Pascal Cubic Meter per Mole --> 200000 Pascal Cubic Meter per Mole No Conversion Required
STEP 2: Evaluate Formula
Substituting Input Values in Formula
xLiquid = ppartial/KH --> 0.2/200000
Evaluating ... ...
xLiquid = 1E-06
STEP 3: Convert Result to Output's Unit
1E-06 --> No Conversion Required
FINAL ANSWER
1E-06 1E-6 <-- Mole Fraction of Component in Liquid Phase
(Calculation completed in 00.004 seconds)

Credits

Created by Shivam Sinha
National Institute Of Technology (NIT), Surathkal
Shivam Sinha has created this Calculator and 300+ more calculators!
Verified by Akshada Kulkarni
National Institute of Information Technology (NIIT), Neemrana
Akshada Kulkarni has verified this Calculator and 900+ more calculators!

20 Ideal Gas Calculators

Work Done in Adiabatic Process using Specific Heat Capacity at Constant Pressure and Volume
Go Work done in Thermodynamic Process = (Initial Pressure of System*Initial Volume of System-Final Pressure of System*Final Volume of System)/((Molar Specific Heat Capacity at Constant Pressure/Molar Specific Heat Capacity at Constant Volume)-1)
Final Temperature in Adiabatic Process (using pressure)
Go Final Temperature in Adiabatic Process = Initial temperature of Gas*(Final Pressure of System/Initial Pressure of System)^(1-1/(Molar Specific Heat Capacity at Constant Pressure/Molar Specific Heat Capacity at Constant Volume))
Final Temperature in Adiabatic Process (using volume)
Go Final Temperature in Adiabatic Process = Initial temperature of Gas*(Initial Volume of System/Final Volume of System)^((Molar Specific Heat Capacity at Constant Pressure/Molar Specific Heat Capacity at Constant Volume)-1)
Work Done in Isothermal Process (using volume)
Go Work done in Thermodynamic Process = Number of Moles of Ideal Gas* [R]*Temperature of Gas*ln(Final Volume of System/Initial Volume of System)
Heat Transferred in Isothermal Process (using Pressure)
Go Heat Transferred in Thermodynamic Process = [R]*Initial temperature of Gas*ln(Initial Pressure of System/Final Pressure of System)
Heat Transferred in Isothermal Process (using Volume)
Go Heat Transferred in Thermodynamic Process = [R]*Initial temperature of Gas*ln(Final Volume of System/Initial Volume of System)
Work done in Isothermal Process (using Pressure)
Go Work done in Thermodynamic Process = [R]*Temperature of Gas*ln(Initial Pressure of System/Final Pressure of System)
Relative Humidity
Go Relative Humidity = Specific Humidity*Partial Pressure/((0.622+Specific Humidity)*Vapor Pressure of Pure Component A)
Heat Transfer in Isobaric Process
Go Heat Transferred in Thermodynamic Process = Number of Moles of Ideal Gas*Molar Specific Heat Capacity at Constant Pressure*Temperature Difference
Heat Transfer in Isochoric Process
Go Heat Transferred in Thermodynamic Process = Number of Moles of Ideal Gas*Molar Specific Heat Capacity at Constant Volume*Temperature Difference
Change in Internal Energy of System
Go Change in Internal Energy = Number of Moles of Ideal Gas*Molar Specific Heat Capacity at Constant Volume*Temperature Difference
Enthalpy of System
Go System Enthalpy = Number of Moles of Ideal Gas*Molar Specific Heat Capacity at Constant Pressure*Temperature Difference
Ideal Gas Law for Calculating Volume
Go Ideal Gas Law for Calculating Volume = [R]*Temperature of Gas/Total Pressure of Ideal Gas
Ideal Gas Law for Calculating Pressure
Go Ideal Gas Law for calculating Pressure = [R]*(Temperature of Gas)/Total Volume of System
Adiabatic Index
Go Heat Capacity Ratio = Molar Specific Heat Capacity at Constant Pressure/Molar Specific Heat Capacity at Constant Volume
Specific Heat Capacity at Constant Pressure
Go Molar Specific Heat Capacity at Constant Pressure = [R]+Molar Specific Heat Capacity at Constant Volume
Specific Heat Capacity at Constant Volume
Go Molar Specific Heat Capacity at Constant Volume = Molar Specific Heat Capacity at Constant Pressure-[R]
Henry Law Constant using Mole Fraction and Partial Pressure of Gas
Go Henry Law Constant = Partial Pressure/Mole Fraction of Component in Liquid Phase
Mole Fraction of Dissolved Gas using Henry Law
Go Mole Fraction of Component in Liquid Phase = Partial Pressure/Henry Law Constant
Partial Pressure using Henry Law
Go Partial Pressure = Henry Law Constant*Mole Fraction of Component in Liquid Phase

Mole Fraction of Dissolved Gas using Henry Law Formula

Mole Fraction of Component in Liquid Phase = Partial Pressure/Henry Law Constant
xLiquid = ppartial/KH

What is Henry’s Law?

Henry’s law is a gas law that states that the amount of gas that is dissolved in a liquid is directly proportional to the partial pressure of that gas above the liquid when the temperature is kept constant. The constant of proportionality for this relationship is called Henry’s law constant.

What is Quasi Static Process?

It is Infinitely slow process. It's Path can be defined. There is no dissipation effects like friction etc. Both System and surroundings can be restored to
their initial state. System follows the same path if we reverse the
process. Quasi static process are also called reversible
process.

How to Calculate Mole Fraction of Dissolved Gas using Henry Law?

Mole Fraction of Dissolved Gas using Henry Law calculator uses Mole Fraction of Component in Liquid Phase = Partial Pressure/Henry Law Constant to calculate the Mole Fraction of Component in Liquid Phase, The Mole fraction of dissolved gas using Henry Law formula is defined as the ratio of the partial pressure of the gas and the Henry law constant. Mole Fraction of Component in Liquid Phase is denoted by xLiquid symbol.

How to calculate Mole Fraction of Dissolved Gas using Henry Law using this online calculator? To use this online calculator for Mole Fraction of Dissolved Gas using Henry Law, enter Partial Pressure (ppartial) & Henry Law Constant (KH) and hit the calculate button. Here is how the Mole Fraction of Dissolved Gas using Henry Law calculation can be explained with given input values -> 3.8E-5 = 0.2/200000.

FAQ

What is Mole Fraction of Dissolved Gas using Henry Law?
The Mole fraction of dissolved gas using Henry Law formula is defined as the ratio of the partial pressure of the gas and the Henry law constant and is represented as xLiquid = ppartial/KH or Mole Fraction of Component in Liquid Phase = Partial Pressure/Henry Law Constant. Partial Pressure is the notional pressure of that constituent gas if it alone occupied the entire volume of the original mixture at the same temperature & Henry Law Constant is a measure of the concentration of a chemical in air over its concentration in water.
How to calculate Mole Fraction of Dissolved Gas using Henry Law?
The Mole fraction of dissolved gas using Henry Law formula is defined as the ratio of the partial pressure of the gas and the Henry law constant is calculated using Mole Fraction of Component in Liquid Phase = Partial Pressure/Henry Law Constant. To calculate Mole Fraction of Dissolved Gas using Henry Law, you need Partial Pressure (ppartial) & Henry Law Constant (KH). With our tool, you need to enter the respective value for Partial Pressure & Henry Law Constant and hit the calculate button. You can also select the units (if any) for Input(s) and the Output as well.
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