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Calculators Created by Vaibhav Mishra
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.
Basic Formulas
(1)
Verified
Discharge Rate of Liquid from Orifice in Tank
Go
6 More Basic Formulas Calculators
Go
Basic Formulas
(2)
Created
Specific Surface Area of Mixture
Go
Created
Total Surface Area of Particle using Spericity
Go
6 More Basic Formulas Calculators
Go
Basics of Heat Transfer
(1)
Created
Logarithmic Mean Area of Cylinder
Go
14 More Basics of Heat Transfer Calculators
Go
Continuous Distillation
(11)
Created
Boil-Up Ratio
Go
Created
Bottom Product based on Boil-up Ratio
Go
Created
Distillate Flowrate based on External Reflux Ratio
Go
Created
Distillate Flowrate based on Internal Reflux Ratio
Go
Created
External Reflux Ratio
Go
Created
Feed Q-Value in Distillation Column
Go
Created
Internal Liquid Reflux Flowrate based on Internal Reflux Ratio
Go
Created
Internal Reflux Ratio
Go
Created
Liquid Reflux Flowrate based on External Reflux Ratio
Go
Created
Minimum Number of Distillation Stages by Fenske's Equation
Go
Created
Vapor Reflux based on Boil-Up Ratio
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2 More Continuous Distillation Calculators
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Diffusivity: Measurement & Prediction
(5)
Created
Chapman Enskog Equation for Gas Phase Diffusivity
Go
Created
Diffusivity by Stefan Tube Method
Go
Created
Diffusivity by Twin Bulb Method
Go
Created
Fuller-Schettler-Giddings for Binary Gas Phase Diffusivity
Go
Created
Wilke Chang Equation for Liquid Phase Diffusivity
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Filtration
(3)
Created
Equivalent Diameter using Reynolds Number
Go
Created
Fraction of Cycle Time used for Cake Formation
Go
Created
Time Required for Cake Formation
Go
Fluidisation
(1)
Created
Pressure Gradient using Kozeny Carman Equation
Go
1 More Fluidisation Calculators
Go
Formulas on Size Reduction Laws
(4)
Created
Area of Product giving Crushing Efficiency
Go
Created
Maximum Diameter of Particle Nipped by Rolls
Go
Created
Radius of Crushing Rolls
Go
Created
Work required for Reduction of Particles
Go
6 More Formulas on Size Reduction Laws Calculators
Go
Gas Absorption
(10)
Created
Absorption Factor
Go
Created
Absorption Factor given Stripping Factor
Go
Created
Gas Flowrate for Absorption Column on Solute Free Basis
Go
Created
Liquid Flowrate for Absorption Column on Solute Free basis
Go
Created
Maximum Gas Rate for Absorption Column
Go
Created
Minimum Liquid Rate for Absorption Column
Go
Created
Minimum Operating Line Slope for Absorption Column
Go
Created
Number of Absorption Stages by Kremser Equation
Go
Created
Number of Stages for Absorption Factor Equal to 1
Go
Created
Operating Line Slope for Absorption Column
Go
Gas Absorption & Stripping
(11)
Created
Corrected Murphree Efficiency Percentage for Liquid Entrainment
Go
Created
Gas Flowrate on Solute Free Basis for Inlet Conditions by Mole Fraction
Go
Created
Gas Flowrate on Solute Free Basis for Inlet Conditions by Solute Free Mole Fraction
Go
Created
Liquid Flowrate on Solute Free Basis for Inlet Conditions by Solute Free Mole Fraction
Go
Created
Liquid Flowrate on Solute Free Basis for Inlet Conditions using Mole Fraction
Go
Created
Murphree Efficiency of Absorption Operation Based on Point Efficiency for Plug Flow
Go
Created
Murphree Tray Efficiency of Absorption Operation
Go
Created
Overall Tray Efficiency for Absorption Column given Murphree Efficiency
Go
Created
Point Efficiency of Absorption Operation
Go
Created
Solute Free Mole Fraction of Gas in Inlet based on Mole Fraction
Go
Created
Solute Free Mole Fraction of Liquid in Inlet based on Mole Fraction
Go
Liquid-Liquid Extraction
(2)
Created
Mass Ratio of Solute in Extract Phase
Go
Created
Mass Ratio of Solute in Raffinate Phase
Go
Mass Transfer Theories
(20)
Created
Average Contact Time by Penetration Theory
Go
Created
Average Mass Transfer Coefficient by Penetration Theory
Go
Created
Diffusivity by Average Contact Time in Penetration Theory
Go
Created
Diffusivity by Film Theory
Go
Created
Diffusivity by Instanataneous Contact Time in Penetration Theory
Go
Created
Diffusivity by Surface Renewal Theory
Go
Created
Film Thickness by Film Theory
Go
Created
Fractional Resistance Offered by Gas Phase
Go
Created
Fractional Resistance Offered by Liquid Phase
Go
Created
Gas Phase Mass Transfer Coefficient by Two Film Theory
Go
Created
Gas Phase Mass Transfer Coefficient using Fractional Resistance by Gas Phase
Go
Created
Instantaneous Contact Time by Penetration Theory
Go
Created
Instantaneous Mass Transfer Coefficient by Penetration Theory
Go
Created
Liquid Phase Mass Transfer Coefficient by Two Film Theory
Go
Created
Liquid Phase Mass Transfer Coefficient using Fractional Resistance by Liquid Phase
Go
Created
Mass Transfer Coefficient by Film Theory
Go
Created
Mass Transfer Coefficient by Surface Renewal Theory
Go
Created
Overall Gas Phase Mass Transfer Coefficient using Fractional Resistance by Gas Phase
Go
Created
Overall Liquid Phase Mass Transfer Coefficient using Fractional Resistance by Liquid Phase
Go
Created
Surface Renewal Rate by Surface Renewal Theory
Go
Material Balance
(14)
Created
Mole Fraction of MVC in Distillate from Overall and Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Distillate from Overall Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Feed from Overall and Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Feed from Overall Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Residue from Overall and Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Residue from Overall Component Material Balance in Distillation
Go
Created
Total Distillate Flowrate of Distillation Column from Overall and Component Material Balance
Go
Created
Total Distillate Flowrate of Distillation Column from Overall Component Material Balance
Go
Created
Total Distillate Flowrate of Distillation Column from Overall Material Balance
Go
Created
Total Feed Flowrate of Distillation Column from Overall Component Material Balance
Go
Created
Total Feed Flowrate of Distillation Column from Overall Material Balance
Go
Created
Total Residue Flowrate of Distillation Column from Overall and Component Material Balance
Go
Created
Total Residue Flowrate of Distillation Column from Overall Component Material Balance
Go
Created
Total Residue Flowrate of Distillation Column from Overall Material Balance
Go
Mechanical Separation
(2)
Created
Combined Overall Efficiency of Screen
Go
Created
Screen Effectiveness based on Oversize Material from Overall Efficiency
Go
10 More Mechanical Separation Calculators
Go
Relative Volatility & Vaporization Ratio
(7)
Created
Equilibrium Vaporization Ratio for Less Volatile Component
Go
Created
Equilibrium Vaporization Ratio for More Volatile Component
Go
Created
Mole Fraction of LVC in Liquid using Equilibrium Vaporization Ratio
Go
Created
Mole Fraction of LVC in Vapor using Equilibrium Vaporization Ratio
Go
Created
Mole Fraction of MVC in Liquid using Equilibrium Vaporization Ratio
Go
Created
Mole Fraction of MVC in Vapor using Equilibrium Vaporization Ratio
Go
Created
Relative Volatility using Equilibrium Vaporization Ratio
Go
3 More Relative Volatility & Vaporization Ratio Calculators
Go
Size Separation
(1)
Created
Projected Area of Solid Body
Go
1 More Size Separation Calculators
Go
Sphericity of Particles
(1)
Created
Surface Shape Factor
Go
3 More Sphericity of Particles Calculators
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Steam Distillation
(5)
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
Go
Created
Moles of Volatile component Volatilized from mixture of Non-Volatiles by Steam at Equilibrium
Go
Created
Total Steam Required to Vaporize Volatile Component
Go
Stripping
(3)
Created
Number of Stripping Stages by Kremser Equation
Go
Created
Stripping Factor
Go
Created
Stripping Factor given Absorption Factor
Go
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