Calculators Created by Vaibhav Mishra

Verified Discharge Rate of Liquid from Orifice in Tank

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8 More Basic Formulas Calculators

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Created Specific Surface Area of Mixture

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Created Total Surface Area of Particle using Spericity

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6 More Basic Formulas Calculators

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Created Logarithmic Mean Area of Cylinder

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16 More Basics of Heat Transfer Calculators

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Created Boil-Up Ratio

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Created Bottom Product based on Boil-up Ratio

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Created Distillate Flowrate based on External Reflux Ratio

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Created Distillate Flowrate based on Internal Reflux Ratio

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Created External Reflux Ratio

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Created Feed Q-Value in Distillation Column

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Created Internal Liquid Reflux Flowrate based on Internal Reflux Ratio

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Created Internal Reflux Ratio

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Created Liquid Reflux Flowrate based on External Reflux Ratio

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Created Minimum Number of Distillation Stages by Fenske's Equation

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Created Vapor Reflux based on Boil-Up Ratio

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2 More Continuous Distillation Calculators

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Created Chapman Enskog Equation for Gas Phase Diffusivity

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Created Diffusivity by Stefan Tube Method

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Created Diffusivity by Twin Bulb Method

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Created Fuller-Schettler-Giddings for Binary Gas Phase Diffusivity

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Created Wilke Chang Equation for Liquid Phase Diffusivity

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Created Distribution Coefficient of Carrier Liquid from Activity Coefficients

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Created Distribution Coefficient of Carrier Liquid from Mole Fraction

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Created Distribution Coefficient of Solute from Activity Coefficient

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Created Distribution Coefficient of Solute from Mole Fractions

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Created Mass Ratio of Solute in Extract Phase

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Created Mass Ratio of Solute in Raffinate Phase

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Created Mass Ratio of Solvent in Extract Phase

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Created Mass Ratio of Solvent in Raffinate Phase

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Created Recovery of Solute in Liquid-Liquid Extraction

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Created Selectivity of Solute based on Distribution Coefficients

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Created Selectvity of Solute based on Activity Coefficients

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Created Selectvity of Solute based on Mole Fractions

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Created Feed Solute Concentration for N-number of Ideal Stage Extraction

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Created Feed Solute Concentration for Single Ideal Stage Extraction

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Created Number of Ideal Equilibrium Extraction Stages

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Created Raffinate Phase Solute Concentration for N Number of Ideal Stage Extraction

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Created Raffinate Phase Solute Concentration for Single Ideal Stage Extraction

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Created Molar Flux of Diffusing Component A for Equimolar Diffusion with B based on Concentration of A

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2 More Equimolar Counter Diffusion Calculators

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Created Equivalent Diameter using Reynolds Number

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Created Fraction of Cycle Time used for Cake Formation

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Created Time Required for Cake Formation

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Created Pressure Gradient using Kozeny Carman Equation

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1 More Fluidisation Calculators

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Created Area of Product giving Crushing Efficiency

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Created Maximum Diameter of Particle Nipped by Rolls

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Created Radius of Crushing Rolls

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Created Work required for Reduction of Particles

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6 More Formulas on Size Reduction Laws Calculators

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Created Absorption Factor

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Created Absorption Factor given Stripping Factor

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Created Gas Flowrate for Absorption Column on Solute Free Basis

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Created Liquid Flowrate for Absorption Column on Solute Free basis

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Created Maximum Gas Rate for Absorption Column

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Created Minimum Liquid Rate for Absorption Column

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Created Minimum Operating Line Slope for Absorption Column

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Created Number of Absorption Stages by Kremser Equation

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Created Number of Stages for Absorption Factor Equal to 1

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Created Operating Line Slope for Absorption Column

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Created Corrected Murphree Efficiency Percentage for Liquid Entrainment

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Created Gas Flowrate on Solute Free Basis for Inlet Conditions by Mole Fraction

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Created Gas Flowrate on Solute Free Basis for Inlet Conditions by Solute Free Mole Fraction

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Created Liquid Flowrate on Solute Free Basis for Inlet Conditions by Solute Free Mole Fraction

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Created Liquid Flowrate on Solute Free Basis for Inlet Conditions using Mole Fraction

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Created Murphree Efficiency of Absorption Operation Based on Point Efficiency for Plug Flow

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Created Murphree Tray Efficiency of Absorption Operation

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Created Overall Tray Efficiency for Absorption Column given Murphree Efficiency

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Created Point Efficiency of Absorption Operation

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Created Solute Free Mole Fraction of Gas in Inlet based on Mole Fraction

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Created Solute Free Mole Fraction of Liquid in Inlet based on Mole Fraction

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Created Extraction Factor at Feed Point Slope of Equilibrium Curve

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Created Extraction Factor at Mean Slope of Equilibrium Curve

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Created Extraction Factor based on Raffinate Point Slope

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Created Geometric Mean of Equilibrium Line Slope

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Created Number of Extraction Stages by Kremser Equation

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Created Number of Stages for Extraction Factor equal to 1

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Created Area of Contact for Batch Leaching Operation

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Created Concentration of Saturated Solution in Contact with Solid

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Created Concentration of Solute in Bulk Solution at Time t

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Created Mass Transfer Coefficient for Batch Leaching

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Created Time of Batch Leaching Operation

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Created Volume of Leaching Solution

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Created Average Contact Time by Penetration Theory

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Created Average Mass Transfer Coefficient by Penetration Theory

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Created Diffusivity by Average Contact Time in Penetration Theory

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Created Diffusivity by Film Theory

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Created Diffusivity by Instanataneous Contact Time in Penetration Theory

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Created Diffusivity by Surface Renewal Theory

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Created Film Thickness by Film Theory

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Created Fractional Resistance Offered by Gas Phase

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Created Fractional Resistance Offered by Liquid Phase

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Created Gas Phase Mass Transfer Coefficient by Two Film Theory

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Created Gas Phase Mass Transfer Coefficient using Fractional Resistance by Gas Phase

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Created Instantaneous Contact Time by Penetration Theory

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Created Instantaneous Mass Transfer Coefficient by Penetration Theory

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Created Liquid Phase Mass Transfer Coefficient by Two Film Theory

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Created Liquid Phase Mass Transfer Coefficient using Fractional Resistance by Liquid Phase

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Created Mass Transfer Coefficient by Film Theory

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Created Mass Transfer Coefficient by Surface Renewal Theory

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Created Overall Gas Phase Mass Transfer Coefficient using Fractional Resistance by Gas Phase

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Created Overall Liquid Phase Mass Transfer Coefficient using Fractional Resistance by Liquid Phase

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Created Surface Renewal Rate by Surface Renewal Theory

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Created Mole Fraction of MVC in Distillate from Overall and Component Material Balance in Distillation

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Created Mole Fraction of MVC in Distillate from Overall Component Material Balance in Distillation

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Created Mole Fraction of MVC in Feed from Overall and Component Material Balance in Distillation

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Created Mole Fraction of MVC in Feed from Overall Component Material Balance in Distillation

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Created Mole Fraction of MVC in Residue from Overall and Component Material Balance in Distillation

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Created Mole Fraction of MVC in Residue from Overall Component Material Balance in Distillation

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Created Total Distillate Flowrate of Distillation Column from Overall and Component Material Balance

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Created Total Distillate Flowrate of Distillation Column from Overall Component Material Balance

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Created Total Distillate Flowrate of Distillation Column from Overall Material Balance

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Created Total Feed Flowrate of Distillation Column from Overall Component Material Balance

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Created Total Feed Flowrate of Distillation Column from Overall Material Balance

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Created Total Residue Flowrate of Distillation Column from Overall and Component Material Balance

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Created Total Residue Flowrate of Distillation Column from Overall Component Material Balance

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Created Total Residue Flowrate of Distillation Column from Overall Material Balance

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Created Combined Overall Efficiency of Screen

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Created Screen Effectiveness based on Oversize Material from Overall Efficiency

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10 More Mechanical Separation Calculators

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Created Equilibrium Vaporization Ratio for Less Volatile Component

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Created Equilibrium Vaporization Ratio for More Volatile Component

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Created Mole Fraction of LVC in Liquid using Equilibrium Vaporization Ratio

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Created Mole Fraction of LVC in Vapor using Equilibrium Vaporization Ratio

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Created Mole Fraction of MVC in Liquid using Equilibrium Vaporization Ratio

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Created Mole Fraction of MVC in Vapor using Equilibrium Vaporization Ratio

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Created Relative Volatility using Equilibrium Vaporization Ratio

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3 More Relative Volatility & Vaporization Ratio Calculators

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Created Projected Area of Solid Body

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1 More Size Separation Calculators

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Created Surface Shape Factor

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3 More Sphericity of Particles Calculators

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Created Log Mean Mole Fraction of B

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8 More Steady State Diffusion Calculators

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

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

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

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

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Created Total Steam Required to Vaporize Volatile Component

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Created Number of Stripping Stages by Kremser Equation

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Created Stripping Factor

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Created Stripping Factor given Absorption Factor

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Created Amount of Solvent Decanted

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Created Amount of Solvent Remaining

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Created Beta Value based on Number of Stages and Fraction of Solute

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Created Beta Value based on Original Weight of Solute

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Created Beta Value based on ratio of Solvent

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Created Fraction of Solute as ratio of Solute

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Created Fraction of Solute Remaining based on Beta Value

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Created Fraction of Solute remaining based on Solvent Decanted

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Created Number of Stages based on Original Weight of Solute

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Created Number of Stages based on Solvent Decanted

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Created Number of Stages for Leaching based on Fraction Solute Retained and Beta Value

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Created Original Weight of Solute based on Number of Stages and Beta Value

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Created Original Weight of Solute in Solid before Washing

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Created Solvent Decanted based on Fraction of Solute remaining and Number of Stages

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Created Weight of Solute remaining based on Number of Stages and Beta Value

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Created Weight of Solute remaining in Solid

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1 More Washing Calculators

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List of Calculators by Vaibhav Mishra