Total Steam Required to Vaporize Volatile Component Calculator

✖The Total Pressure of System is the Total Pressure of the Steam Distillation System under Operation.ⓘ Total Pressure of System [P]			+10% -10%
✖The Vaporizing Efficiency is the factor used to take into account the deviation for steam distillation not operating under equilibrium.ⓘ Vaporizing Efficiency [E]			+10% -10%
✖The Vapor Pressure of Volatile Component is the vapor pressure exerted by the Volatile component in a mixture with non-volatiles.ⓘ Vapor Pressure of Volatile Component [Pvapor_vc]			+10% -10%
✖The Initial Moles of Volatile Component is the number of moles of Volatile component present initially in the system.ⓘ Initial Moles of Volatile Component [m_Ai]			+10% -10%
✖The Final Moles of Volatile Component is the amount of moles of volatile component present into the system after the Steam Distillation Process.ⓘ Final Moles of Volatile Component [m_Af]			+10% -10%
✖The Moles of Non-Volatile Component is the number of moles of non-volatile component present in a mixture of volatiles for Steam Distillation.ⓘ Moles of Non-Volatile Component [m_c]			+10% -10%

✖The Total Steam Required to Vaporize Volatile Component in Steam Distillation is the number of moles of Steam Required to vaporize volatile component from initial to final moles.ⓘ Total Steam Required to Vaporize Volatile Component [M_s]

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Total Steam Required to Vaporize Volatile Component Solution

STEP 0: Pre-Calculation Summary

Formula Used

Total Steam Required to Vaporize Volatile Comp = (((Total Pressure of System/(Vaporizing Efficiency*Vapor Pressure of Volatile Component))-1)*(Initial Moles of Volatile Component-Final Moles of Volatile Component))+((Total Pressure of System*Moles of Non-Volatile Component/(Vaporizing Efficiency*Vapor Pressure of Volatile Component))*ln(Initial Moles of Volatile Component/Final Moles of Volatile Component))
M_s = (((P/(E*Pvapor_vc))-1)*(m_Ai-m_Af))+((P*m_c/(E*Pvapor_vc))*ln(m_Ai/m_Af))
This formula uses 1 Functions, 7 Variables

Functions Used

ln - The natural logarithm, also known as the logarithm to the base e, is the inverse function of the natural exponential function., ln(Number)

Variables Used

Total Steam Required to Vaporize Volatile Comp - (Measured in Mole) - The Total Steam Required to Vaporize Volatile Component in Steam Distillation is the number of moles of Steam Required to vaporize volatile component from initial to final moles.
Total Pressure of System - (Measured in Pascal) - The Total Pressure of System is the Total Pressure of the Steam Distillation System under Operation.
Vaporizing Efficiency - The Vaporizing Efficiency is the factor used to take into account the deviation for steam distillation not operating under equilibrium.
Vapor Pressure of Volatile Component - (Measured in Pascal) - The Vapor Pressure of Volatile Component is the vapor pressure exerted by the Volatile component in a mixture with non-volatiles.
Initial Moles of Volatile Component - (Measured in Mole) - The Initial Moles of Volatile Component is the number of moles of Volatile component present initially in the system.
Final Moles of Volatile Component - (Measured in Mole) - The Final Moles of Volatile Component is the amount of moles of volatile component present into the system after the Steam Distillation Process.
Moles of Non-Volatile Component - (Measured in Mole) - The Moles of Non-Volatile Component is the number of moles of non-volatile component present in a mixture of volatiles for Steam Distillation.

STEP 1: Convert Input(s) to Base Unit

Total Pressure of System: 100000 Pascal --> 100000 Pascal No Conversion Required
Vaporizing Efficiency: 0.75 --> No Conversion Required
Vapor Pressure of Volatile Component: 30000 Pascal --> 30000 Pascal No Conversion Required
Initial Moles of Volatile Component: 5.1 Mole --> 5.1 Mole No Conversion Required
Final Moles of Volatile Component: 0.63 Mole --> 0.63 Mole No Conversion Required
Moles of Non-Volatile Component: 2 Mole --> 2 Mole No Conversion Required

STEP 2: Evaluate Formula

Substituting Input Values in Formula

M_s = (((P/(E*Pvapor_vc))-1)*(m_Ai-m_Af))+((P*m_c/(E*Pvapor_vc))*ln(m_Ai/m_Af)) --> (((100000/(0.75*30000))-1)*(5.1-0.63))+((100000*2/(0.75*30000))*ln(5.1/0.63))

Evaluating ... ...

M_s = 33.985786660683

STEP 3: Convert Result to Output's Unit

33.985786660683 Mole --> No Conversion Required

FINAL ANSWER

33.985786660683 ≈ 33.98579 Mole <-- Total Steam Required to Vaporize Volatile Comp

(Calculation completed in 00.004 seconds)

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Created by Vaibhav Mishra

DJ Sanghvi College of Engineering (DJSCE), Mumbai

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< Steam Distillation Calculators

Moles of Volatile component Volatilized from mixture of Non-Volatiles by Steam

LaTeX Go Moles of Volatile Component = Moles of Steam*((Vaporizing Efficiency*Mole Fraction of Volatile Comp in Non-Volatiles*Vapor Pressure of Volatile Component)/(Total Pressure of System-Vaporizing Efficiency*Mole Fraction of Volatile Comp in Non-Volatiles*Vapor Pressure of Volatile Component))

Moles of Volatile component Volatilized from mixture of Non-Volatiles by Steam at Equilibrium

LaTeX Go Moles of Volatile Component = Moles of Steam*(Mole Fraction of Volatile Comp in Non-Volatiles*Vapor Pressure of Volatile Component/(Total Pressure of System-Mole Fraction of Volatile Comp in Non-Volatiles*Vapor Pressure of Volatile Component))

Moles of Volatile component Volatilized by Steam with Trace amounts of Non-Volatiles

LaTeX Go Moles of Volatile Component = Moles of Steam*((Vaporizing Efficiency*Vapor Pressure of Volatile Component)/(Total Pressure of System-(Vaporizing Efficiency*Vapor Pressure of Volatile Component)))

Moles of Volatile component Volatilized by Steam with Trace amounts of Non-Volatiles at Equilibrium

LaTeX Go Moles of Volatile Component = Moles of Steam*(Vapor Pressure of Volatile Component/(Total Pressure of System-Vapor Pressure of Volatile Component))

< Important Formulas in Distillation Mass Transfer Operation Calculators

Feed Q-Value in Distillation Column

LaTeX Go Q-value in Mass Transfer = Heat Required to Convert Feed to Saturated Vapor/Molal Latent Heat of Vaporization of Saturated Liq

External Reflux Ratio

LaTeX Go External Reflux Ratio = External Reflux Flowrate to Distillation Column/Distillate Flowrate from Distillation Column

Internal Reflux Ratio

LaTeX Go Internal Reflux Ratio = Internal Reflux Flowrate to Distillation Column/Distillate Flowrate from Distillation Column

Boil-Up Ratio

LaTeX Go Boil-Up Ratio = Boil-Up Flowrate to the Distillation Column/Residue Flowrate from Distillation Column

Total Steam Required to Vaporize Volatile Component Formula

LaTeX Go

What is Steam Distillation?

Steam distillation is a separation process that consists of distilling water together with other volatile and non-volatile components. The steam from the boiling water carries the vapor of the volatiles to a condenser; both are cooled and return to the liquid or solid state, while the non-volatile residues remain behind in the boiling container. If, as is usually the case, the volatiles are not miscible with water, they will spontaneously form a distinct phase after condensation, allowing them to be separated by decantation or with a separatory funnel.

How to Calculate Total Steam Required to Vaporize Volatile Component?

Total Steam Required to Vaporize Volatile Component calculator uses Total Steam Required to Vaporize Volatile Comp = (((Total Pressure of System/(Vaporizing Efficiency*Vapor Pressure of Volatile Component))-1)*(Initial Moles of Volatile Component-Final Moles of Volatile Component))+((Total Pressure of System*Moles of Non-Volatile Component/(Vaporizing Efficiency*Vapor Pressure of Volatile Component))*ln(Initial Moles of Volatile Component/Final Moles of Volatile Component)) to calculate the Total Steam Required to Vaporize Volatile Comp, The Total Steam Required to Vaporize Volatile Component formula is defined as the total requirement of steam to vaporize the volatile component from an initial mass to final mass of volatile component. Total Steam Required to Vaporize Volatile Comp is denoted by M_s symbol.

How to calculate Total Steam Required to Vaporize Volatile Component using this online calculator? To use this online calculator for Total Steam Required to Vaporize Volatile Component, enter Total Pressure of System (P), Vaporizing Efficiency (E), Vapor Pressure of Volatile Component (Pvapor_vc), Initial Moles of Volatile Component (m_Ai), Final Moles of Volatile Component (m_Af) & Moles of Non-Volatile Component (m_c) and hit the calculate button. Here is how the Total Steam Required to Vaporize Volatile Component calculation can be explained with given input values -> 33.98579 = (((100000/(0.75*30000))-1)*(5.1-0.63))+((100000*2/(0.75*30000))*ln(5.1/0.63)).

FAQ

What is Total Steam Required to Vaporize Volatile Component?

The Total Steam Required to Vaporize Volatile Component formula is defined as the total requirement of steam to vaporize the volatile component from an initial mass to final mass of volatile component and is represented as M_s = (((P/(E*Pvapor_vc))-1)*(m_Ai-m_Af))+((P*m_c/(E*Pvapor_vc))*ln(m_Ai/m_Af)) or Total Steam Required to Vaporize Volatile Comp = (((Total Pressure of System/(Vaporizing Efficiency*Vapor Pressure of Volatile Component))-1)*(Initial Moles of Volatile Component-Final Moles of Volatile Component))+((Total Pressure of System*Moles of Non-Volatile Component/(Vaporizing Efficiency*Vapor Pressure of Volatile Component))*ln(Initial Moles of Volatile Component/Final Moles of Volatile Component)). The Total Pressure of System is the Total Pressure of the Steam Distillation System under Operation, The Vaporizing Efficiency is the factor used to take into account the deviation for steam distillation not operating under equilibrium, The Vapor Pressure of Volatile Component is the vapor pressure exerted by the Volatile component in a mixture with non-volatiles, The Initial Moles of Volatile Component is the number of moles of Volatile component present initially in the system, The Final Moles of Volatile Component is the amount of moles of volatile component present into the system after the Steam Distillation Process & The Moles of Non-Volatile Component is the number of moles of non-volatile component present in a mixture of volatiles for Steam Distillation.

How to calculate Total Steam Required to Vaporize Volatile Component?

The Total Steam Required to Vaporize Volatile Component formula is defined as the total requirement of steam to vaporize the volatile component from an initial mass to final mass of volatile component is calculated using Total Steam Required to Vaporize Volatile Comp = (((Total Pressure of System/(Vaporizing Efficiency*Vapor Pressure of Volatile Component))-1)*(Initial Moles of Volatile Component-Final Moles of Volatile Component))+((Total Pressure of System*Moles of Non-Volatile Component/(Vaporizing Efficiency*Vapor Pressure of Volatile Component))*ln(Initial Moles of Volatile Component/Final Moles of Volatile Component)). To calculate Total Steam Required to Vaporize Volatile Component, you need Total Pressure of System (P), Vaporizing Efficiency (E), Vapor Pressure of Volatile Component (Pvapor_vc), Initial Moles of Volatile Component (m_Ai), Final Moles of Volatile Component (m_Af) & Moles of Non-Volatile Component (m_c). With our tool, you need to enter the respective value for Total Pressure of System, Vaporizing Efficiency, Vapor Pressure of Volatile Component, Initial Moles of Volatile Component, Final Moles of Volatile Component & Moles of Non-Volatile Component 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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