Calculators Created by Vaibhav Mishra

DJ Sanghvi College of Engineering (DJSCE), Mumbai
www.linkedin.com/in/vaibhavmishra2310
103
Formulas Created
1
Formulas Verified
19
Across Categories

List of Calculators by Vaibhav Mishra

Following is a combined list of all the calculators that have been created and verified by Vaibhav Mishra. Vaibhav Mishra has created 103 and verified 1 calculators across 19 different categories till date.
Verified Discharge Rate of Liquid from Orifice in Tank
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6 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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14 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 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 Mass Ratio of Solute in Extract Phase
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Created Mass Ratio of Solute in Raffinate Phase
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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 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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