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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Verified Bundle Diameter for Eight Tube Pass Square Pitch in Heat Exchanger

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Verified Bundle Diameter for Eight Tube Pass Triangular Pitch in Heat Exchanger

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Verified Bundle Diameter for Four Tube Pass Square Pitch in Heat Exchanger

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Verified Bundle Diameter for One Tube Pass Square Pitch in Heat Exchanger

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Verified Bundle Diameter for Six Tube Pass Square Pitch in Heat Exchanger

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Verified Bundle Diameter for Two Tube Pass Square Pitch in Heat Exchanger

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4 More Bundle Diameter in Heat Exchanger 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 Fractional Solute Discharge based on Ratio of Overflow to Underflow

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Created Fractional Solute Discharge based on Recovery of Solute

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Created Fractional Solute Discharge Ratio based on Solute Underflow

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Created Number of Equilibirum Leaching Stages based on Fractional Solute Discharge

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Created Number of Equilibirum Leaching Stages based on Solute Underflow

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Created Number of Equilibrium Leaching Stages based on Recovery of Solute

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Created Ratio of Solute Discharged in Underflow to Overflow

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Created Ratio of Solution Discharged in Overflow to Underflow

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Created Ratio of Solvent Discharged in Underflow to Overflow

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Created Recovery of Solute based on Fractional Solute Discharge

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Created Recovery of Solute based on Solute Underflow

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Created Solute Discharged in Overflow based on Ratio of Overflow to Underflow

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Created Solute Discharged in Overflow based on Ratio of Overflow to Underflow and Solution Discharged

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Created Solute Discharged in Underflow based on Ratio of Overflow to Underflow

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Created Solute Discharged in Underflow based on Ratio of Overflow to Underflow and Solution Discharged

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Created Solute Underflow Entering Column based on Fractional Solute Discharge

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Created Solute Underflow Entering Column based on Ratio of Overflow to Underflow

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Created Solute Underflow Entering Column based on Recovery of Solute

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Created Solute Underflow Leaving Column based on Fractional Solute Discharge

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Created Solute Underflow Leaving Column based on Ratio of Overflow to Underflow

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Created Solute Underflow Leaving Column based on Recovery of Solute

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Created Solution Discharged in Overflow based on Ratio of Overflow to Underflow

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Created Solution Discharged in Overflow based on Ratio of Overflow to Underflow and Solute Discharged

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Created Solution Discharged in Underflow based on Ratio of Overflow to Underflow

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Created Solution Discharged in Underflow based on Ratio of Overflow to Underflow and Solute Discharged

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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 Mass Fraction

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Created Distribution Coefficient of Solute from Activity Coefficient

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Created Distribution Coefficient of Solute from Mass 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 Dry Weight of Solid based on Critical to Final Moisture Content for Falling Rate Period

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Created Drying Surface Area based on Critical to Final Moisture Content for Falling Rate Period

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Created Drying Surface Area based on Critical to Final Weight of Moisture for Falling Rate Period

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Created Falling Rate Drying Time from Critical to Final Moisture

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Created Falling Rate Drying Time from Critical to Final Weight of Moisture

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Created Final Moisture Content based on Critical to Final Moisture Content for Falling Rate Period

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Created Final Weight of Moisture based on Critical to Final Weight of Moisture for Falling Rate Period

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Created Rate of Constant Drying Period based on Critical to Final Moisture Content for Falling Rate Period

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Created Rate of Constant Drying Period based on Critical to Final Weight of Moisture for Falling Rate Period

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Created Constant Drying Time from Initial to Critical Moisture Content

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Created Constant Drying Time from Initial to Critical Weight of Moisture

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Created Critical Moisture Content based on Initial Moisture Content for Constant Rate Period

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Created Critical Weight of Moisture based on Initial Weight of Moisture for Constant Rate Period

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Created Dry Weight of Solid from Initial to Critical Moisture Content for Constant Rate Period

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Created Drying Surface Area based on Initial to Critical Moisture Content for Constant Rate Period

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Created Drying Surface Area based on Initial to Critical Weight of Moisture for Constant Rate Period

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Created Initial Moisture Content based on Critical Moisture Content for Constant Rate Period

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Created Initial Weight of Moisture based on Critical Weight of Moisture for Constant Rate Period

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Created Rate of Constant Drying Period based on Critical Moisture Content

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Created Rate of Constant Drying Period based on Critical Weight of Moisture

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Created Constant Drying Time from Initial to Final Moisture Content

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Created Constant Drying Time from Initial to Final Weight of Moisture

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Created Dry Weight of Solid from Initial to Final Moisture Content for Constant Rate Period

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Created Drying Surface Area based on Initial to Final Moisture Content for Constant Rate Period

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Created Drying Surface Area based on Initial to Final Weight of Moisture for Constant Rate Period

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Created Final Moisture Content based on Initial Moisture Content for Constant Rate Period

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Created Final Weight of Moisture based on Initial Weight of Moisture for Constant Rate Period

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Created Initial Moisture Content based on Final Moisture Content for Constant Rate Period

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Created Initial Weight of Moisture based on Final Weight of Moisture for Constant Rate Period

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Created Rate of Constant Drying Period based on Final Moisture Content

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Created Rate of Constant Drying Period based on Final Weight of Moisture

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Created Dry Weight of Solid based on Initial to Final Moisture Content for Falling Rate Period

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Created Drying Surface Area based on Initial to Final Moisture Content for Falling Rate Period

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Created Drying Surface Area based on Initial to Final Weight of Moisture for Falling Rate Period

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Created Falling Rate Drying Time from Initial to Final Moisture

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Created Falling Rate Drying Time from Initial to Final Weight of Moisture

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Created Final Moisture Content based on Initial to Final Moisture Content for Falling Rate Period

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Created Final Weight of Moisture based on Initial to Final Weight of Moisture for Falling Rate Period

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Created Rate of Constant Drying Period based on Initial to Final Moisture Content for Falling Rate Period

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Created Rate of Constant Drying Period based on Initial to Final Weight of Moisture for Falling Rate Period

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Created Constant Drying Time based on Total Drying Time and Falling Drying Time

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Created Falling Drying Time based on Constant Drying Time and Total Drying Time

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Created Total Drying Time based on Constant Drying Time and Falling Drying Time

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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 Maximum Intermediate Concentration in First Order followed by Zero Order Reaction

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9 More First Order followed by Zero Order Reaction Calculators

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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 given 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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Verified Shell Diameter of Heat Exchanger Given Clearance and Bundle Diameter

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21 More Heat Exchangers Calculators

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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 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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Verified Hagen Poiseuille Based Flux for Membrane Separation

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12 More Membrane Separation Calculators

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Created Bound Moisture Content based on Free and Equilibrium Moisture Content

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Created Bound Moisture Content based on Unbound Moisture Content

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Created Equilibrium Moisture Content based on Bound and Unbound Moisture Content

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Created Equilibrium Moisture Content based on Free Moisture Content

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Created Free Moisture Content based on Bound and Unbound Moisture Content

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Created Free Moisture Content based on Equilibrium Moisture Content

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Created Initial Moisture Content based on Bound and Unbound Moisture Content

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Created Initial Moisture Content based on Free and Equlibrium Moisture Content

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Created Unbound Moisture Content based on Bound Moisture Content

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Created Unbound Moisture Content based on Free and Equilibrium Moisture Content

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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 in Batch Leaching

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Created Concentration of Solute in Bulk Solution at Time t for Batch Leaching

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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 in Batch Leaching

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Verified Diesel Index

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8 More Petrochemicals Calculators

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Created Bound Moisture Content based on Weight of Bound Moisture

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Created Critical Moisture Content based on Weight of Critical Moisture

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Created Dry Weight of Solid based on Bound Moisture Content

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Created Dry Weight of Solid based on Critical Moisture Content

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Created Dry Weight of Solid based on Equilibrium Moisture Content

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Created Dry Weight of Solid based on Free Moisture Content

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Created Dry Weight of Solid based on Initial Moisture Content

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Created Dry Weight of Solid based on Unbound Moisture Content

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Created Equilibrium Moisture Content based on Weight of Equilibrium Moisture

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Created Free Moisture Content based on Weight of Free Moisture

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Created Initial Moisture Content based on Weight of Initial Moisture

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Created Unbound Moisture Content based on Weight of Unbound Moisture

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Created Weight of Bound Moisture based on Bound Moisture Content

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Created Weight of Critical Moisture based on Critical Moisture Content

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Created Weight of Equilibrium Moisture based on Equilibrium Moisture Content

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Created Weight of Free Moisture based on Free Moisture Content

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Created Weight of Initial Moisture based on Initial Moisture Content

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Created Weight of Unbound Moisture based on Unbound Moisture Content

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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 Amount of Solvent Decanted

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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 Solvent Decanted based on Original Weight of Solute and Number of Stages

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

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Created Solvent Remaining based on Original Weight of Solute and Number of Stages

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Created Weight of Solute remaining based on Number of Stages and Amount of Solvent Decanted

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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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Created Bound Moisture Weight based on Free and Equilibrium Moisture Weight

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Created Bound Moisture Weight based on Unbound Moisture Weight

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Created Equilibrium Moisture Weight based on Bound and Unbound Moisture Weight

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Created Equilibrium Moisture Weight based on Free Moisture Weight

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Created Free Moisture Weight based on Bound and Unbound Moisture Weight

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Created Free Moisture Weight based on Equilibrium Moisture Weight

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Created Initial Moisture based on Free and Equlibrium Moisture Weight

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Created Initial Moisture Weight based on Bound and Unbound Moisture Weight

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Created Unbound Moisture Weight based on Bound Moisture Weight

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Created Unbound Moisture Weight based on Free and Equilibrium Moisture Weight

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List of Calculators by Vaibhav Mishra