Calculators Created by Vaibhav Mishra

DJ Sanghvi College of Engineering (DJSCE), Mumbai
www.linkedin.com/in/vaibhavmishra2310
285
Formulas Created
207
Formulas Verified
63
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 285 and verified 207 calculators across 63 different categories till date.
Created Adiabatic Saturation Temperature
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Created Air Humidity at Wet Bulb Temperature based on Heat and Mass Transfer Rates
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Created Air Inlet Temperature based on Adiabatic Saturation Temperature
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Created Ambient Air Humidity based on Wet Bulb Temperature
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Created Ambient Air Temperature based on Wet Bulb Temperature
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Created Heat Transfer Coefficient based on Wet Bulb Temperature
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Created Humid Heat of Air based on Adiabatic Saturation Temperature
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Created Inlet Air Humidity based on Adiabatic Saturation Temperature
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Created Latent Heat of Air based on Adiabatic Saturation Temperature
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Created Latent Heat of Air based on Wet Bulb Temperature
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Created Mass Transfer Coefficient based on Wet Bulb Temperature
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Created Saturated Exit Air Humidity based on Adiabatic Saturation Temperature
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Created Wet Bulb Temperature
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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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7 More Basic Formulas Calculators
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Verified Allowable Length of Tube given Temperature Difference and Thermal Expansion of Tubes
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Verified Baffle Spacing given Tube Length and Number of Baffles
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Verified Bundle Diameter given Number of Tubes in Centre Row and Pitch
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Verified Channel Velocity of Fluid given Path Length and Plate Pressure Drop
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Verified Heat Duty of Exchanger given Core Volume of Exchanger for Air Separation
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Verified Heat Duty of Exchanger given Core Volume of Exchanger for Hydrocarbon Separation
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Verified Log Mean Temperature Difference in Plate Heat Exchanger Given Fluid Temperature and NTU
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Verified Number of Tubes in Eight Pass Square Pitch given Bundle Diameter
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Verified Number of Tubes in Eight Pass Triangular Pitch given Bundle Diameter
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Verified Number of Tubes in Four Pass Square Pitch given Bundle Diameter
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Verified Number of Tubes in Four Pass Triangular Pitch given Bundle Diameter
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Verified Number of Tubes in One Pass Square Pitch given Bundle Diameter
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Verified Number of Tubes in One Pass Triangular Pitch given Bundle Diameter
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Verified Number of Tubes in Six Pass Square Pitch given Bundle Diameter
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Verified Number of Tubes in Six Pass Triangular Pitch given Bundle Diameter
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Verified Number of Tubes in Two Pass Square Pitch given Bundle Diameter
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Verified Number of Tubes in Two Pass Triangular Pitch given Bundle Diameter
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Verified Outlet Temperature of Fluid in Plate Heat Exchanger given NTU and Log Mean Temperature Difference
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Verified Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop
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Verified Pressure Drop in Plate Type Heat Exchanger
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Verified Shell Diameter of Heat Exchanger Given Clearance and Bundle Diameter
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Verified Temperature Difference Achieved given Thermal Expansion and Length of Tubes in Heat Exchanger
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Verified Tube Side Mass Flowrate Given Pumping Power and Tube Side Pressure Drop
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Verified Tube Side Mass Flowrate of Liquid Given Number of Tubes and Fluid Velocity
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Verified Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid
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Verified Tube Side Velocity of Fluid Given Mass Flowrate and Number of Tubes
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25 More Basic Formulas Of Heat Exchanger Designs 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 Absolute Humidity based on Humid Heat
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Created Absolute Humidity based on Humid Volume and Temperature
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Created Absolute Humidity based on Percentage and Saturation Humidity
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Created Humid Volume based on Absolute Humidity and Temperature
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Created Molal Humidity based on Absolute Humidity
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Created Moles of Air based on Molal Humidity
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Created Moles of Water Vapour based on Molal Humidity
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Created Saturation Humidity based on Percentage and Absolute Humidity
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Created Temperature based on Absolute Humidity and Humid Volume
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Created Weight of Air based on Absolute Humidity
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Created Weight of Water Vapour based on Absolute Humidity
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8 More Basics of Humidification Process Calculators
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Verified Applied Pressure Driving Force Based on Permeability of Membrane
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Verified Concentration of Mass at Membrane Surface
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Verified Hagen Poiseuille Based Flux for Membrane Separation
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Verified Liquid Flow through Pore Based On Poiseuilles Law
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Verified Liquid Viscosity based on Membrane Resistance
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Verified Liquid Viscosity based on Poiseuille's Law
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Verified Membrane Flux Based on Resistance
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Verified Membrane Flux Based on Water Permeability
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Verified Partial Molar Volume of Water based on Solution Diffusion Model
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Verified Pressure Difference across Pore based on Poiseuille's Law
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Verified Resistance to flow in Membranes
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Verified Time of Dialysis using Hollow Fiber Haemodialyser
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Verified Water Permeability based on Initial flux
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Verified Water Permeability through Membrane
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2 More Basics of Membrane Separation Processes Calculators
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Verified Diesel Index
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Verified Melt Flow Index
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7 More Basics of Petrochemicals 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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Verified Fixed Capital Investment
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Verified Fixed Cost at Breakeven Point
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Verified Total Production Cost Considering Fixed Cost and Variable Cost
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Verified Working Capital Investment
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7 More Cost Estimation 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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Verified Equilibrium Saturation Value given Relative Supersaturation and Degree of Saturation
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Verified Mass Flux Density given Mass Transfer Coefficient and Concentration Gradient
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Verified Mass Flux Density given Reaction Rate Constant and Order of Integration Reaction
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Verified Mass Transfer Coefficient given Mass Flux Density and Concentration Gradient
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Verified Nucleation Rate for given Number of Particles and Volume of Constant Supersaturation
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Verified Overall Excess Free Energy for Spherical Crystalline Body
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Verified Reaction Rate Constant in Crystallization given Mass Flux Density and Order of Reaction
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Verified Relative Supersaturation for given Supersaturation Ratio
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Verified Relative Supersaturation given Degree of Saturation and Equilibrium Saturation Value
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Verified Solubility Product given Activities of Species A and B
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Verified Solubility Product given Concentration of Species A and B
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Verified Supersaturation based on activities of Species A and B
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Verified Supersaturation based on Concentration of Species A and B along with Solubility Product
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Verified Supersaturation Ratio given Solution Concentration and Equilibrium Saturation Value
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Verified Supersaturation Time given Nucleation Rate and Supersaturation Volume
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Verified Supersaturation Volume given Nucleation Rate and Supersaturation Time
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Verified Suspension Density given Solid Density and Volumetric Holdup
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7 More Crystallization Calculators
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Verified Activity of Catalyst
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Verified Deactivation rate for Batch Solids and Mixed Changing Flow of Fluids
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Verified Deactivation Rate for Batch Solids and Plug Changing Flow of Fluids
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Verified Deactivation rate for Batch Solids and Plug Constant Flow of Fluids
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Verified Deactivation Rate in Batch Solids and Mixed Constant Flow of Fluids
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Verified Initial Reactant Concentration of Reactant for No Pore Resistance in Catalyst Deactivation
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Verified Rate Constant based on Weight of Catalyst in Batch Solids and Mixed Constant Flow of Fluids
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Verified Volume of Reactor for Batch Solids and Batch Fluids
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Verified Weight of Catalyst in Batch Solids and Batch Fluids
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6 More Deactivating Catalysts Calculators
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Verified Annual Depreciation by Straight-Line Method
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Verified Asset Value after 'a' Years
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Verified Asset Value using Declining Balance Method
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Verified Book Value of Process Equipment at any Time during Service Life
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Verified Depletion Cost
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Verified Depreciation by Sum of Year Digit Method
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Verified Fixed Percentage Factor using Matheson Formula
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Verified Replacement Value by Sinking Fund Method
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Verified Length of Key based on Crushing Stress in Key
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Verified Thickness of Key based on Crushing Stress
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6 More Design of Key Calculators
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Verified Internal Pressure of Cylindrical Vessel given Hoop Stress
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Verified Internal Presure of Vessel given Longitudinal Stress
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Verified Wall Thickness of Cylindrical Shell Given Hoop Stress
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Verified Wall Thickness of Pressure Vessel given Longitudinal Stress
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13 More Design of Pressure Vessel Subjected to Internal Pressure 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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Verified Dispersion Coefficient based on Variance of Spread of Tracer at Small Extents of Dispersion
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Verified Length of Spread based on Variance of Spread of Tracer for Small Extents of Dispersion
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Verified Mean Residence Time where Dispersion Number is less than 0.01
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Verified Standard Deviation of Tracer based on Mean Residence Time for Large Deviations of Dispersion
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5 More Dispersion Model Calculators
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Verified Active Area Given Total Area and Fractional Downcomer Area
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Verified Clearance Area under Downcomer given Weir Length and Apron Height
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Verified Column Diameter given Maximum Vapor Rate and Maximum Vapor Velocity
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Verified Downcomer Liquid Load in Trays
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Verified Downcomer Residence Time in Distillation Column
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Verified Dry Plate Pressure Drop in Distillation Column Design
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Verified External Reflux Ratio given Internal Reflux Ratio
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Verified Flooding Velocity for given Flooding Constant
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Verified Flooding Velocity in Distillation Column Design
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Verified Head Loss in Downcomer of Tray Tower
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Verified Height of Liquid Crest over Weir
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Verified Length of Weir given Clearance Area and Apron Height of Tray
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Verified Liquid Flowrate in Rectifying Section for given Quality of Feed
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Verified Liquid Flowrate over Tray for given Dowcomer Liquid Load
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Verified Liquid Vapor Flow Factor in Distillation Column Design
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Verified Maximum Allowable Vapor Velocity given Plate Spacing and Fluid Densities
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Verified Quality of Feed based on Enthalpy of Feed and Latent Heat of Vaporization
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Verified Quality of Feed Based on Liquid Flowrates and Feed Flowrate
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Verified Rectifying Section Flowrate of Liquid for given Quality of Feed
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Verified Rectifying Section Flowrate of Vapor for given Quality of Feed
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Verified Residual Head Loss in Pressure in Distillation Column
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Verified Souders and Brown Flooding Constant
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Verified Stripping Section Flowrate of Liquid for given Quality of Feed
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Verified Stripping Section Flowrate of Vapor for given Quality of Feed
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Verified Vapor Flowrate in Rectifying Section for given Quality of Feed
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Verified Weep Fraction of Tray
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Verified Weep Point Velocity in Distillation Column Design
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14 More Distillation Tower Design Calculators
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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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Verified Initial Reactant Concentration of Microfluid treated in Mixed Flow Reactor
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Verified Life of Element in Fluid
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Verified Reactant Concentration of Macrofluid in Mixed Flow Reactor at First Order
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Verified Reactant Concentration of Macrofluid in Mixed Flow Reactor at Zero Order
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Verified Reactant Concentration of Microfluid and Macrofluid in Plug Flow Reactor at Second Order
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4 More Earliness of Mixing,Segregation,RTD Calculators
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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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Verified Total Cycle 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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Verified Dynamic Viscosity based on Kozeny Carman Equation
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Created Pressure Gradient using Kozeny Carman Equation
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Verified Total Volume of Bed Based on Porosity
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Verified Volume of Voids in Bed Based on Porosity
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1 More Fluidisation Calculators
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Created Area of Product given Crushing Efficiency
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Verified Feed Rate to Machine for Size Reduction of Particles
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Created Maximum Diameter of Particle Nipped by Rolls
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Verified Power Consumption by Mill while Crushing
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Verified Power Required by Machine for Size Reduction of Particles
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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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Verified Concentration of Reactant B at Extreme A
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Verified Concentration of Reactant B in G/L Reactions
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Verified Henry's Law Constant
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Verified Inner Area of Particle
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Verified Liquid Holdup
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Verified Rate Equation of Reactant A in G/L Reactions
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Verified Rate Equation of Reactant B in G/L Reactions
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Verified Solid Loading
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5 More G/L Reactions on Solid Catalysts 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 Heat Transfer Coefficient with Tube Loading for Condensation Inside Vertical Tubes
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Verified Heat Transfer Coefficient with Tube Loading for Condensation Outside Horizontal Tubes
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Verified Heat Transfer Coefficient with Tube Loading for Condensation Outside Vertical Tubes
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Verified Horizontal Tube Loading for Outside Condensation
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Verified Length of Tubes in Horizontal Condenser given Tube Loading and Condensate Flowrate
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Verified Number of Tubes in Horizontal Condenser given Condensate Flowrate and Tube Loading
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Verified Reynolds Number for Condensate Film given Tube Loading
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Verified Vertical Tube Loading for Inside Condensation
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Verified Vertical Tube Loading for Outside Condensation
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Verified Vertical Tube Loading given Reynolds Number for Condensate Film
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9 More Heat Transfer Coefficient in Heat Exchangers Calculators
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Verified Feed Diameter based on Reduction Law
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Verified Power Consumption while Mill is Empty
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Verified Product Diameter Based on Reduction Ratio
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16 More Important Formulas in Size Reduction Laws 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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Verified Membrane Water Concentration Based on Solution Diffusion Model
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Created Vapor Pressure of Water using Saturation Humidity
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1 More Manometers Calculators
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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 Bulk Concentration of Membrane
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Verified Initial Flux of Membrane
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Verified Initial Membrane Volume
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Verified Membrane Pressure Drop
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Verified Membrane Pressure Drop Based On Solution Diffusion Model
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Verified Membrane Thickness
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Verified Membrane Thickness Based on Solution Diffusion Model
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Verified Osmotic Pressure Drop Based on Solution Diffusion Model
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Verified Pressure Driving Force in Membrane
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4 More Membrane Characteristics 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 Effective Interfacial Area of Packing using Onda's Method
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Verified Gas Film Mass Transfer Coefficient given Column Performance and Interfacial Area
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Verified Gas Flowrate given Column Performance and Interfacial Area
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Verified Gas Molar Flux given Height of Transfer Unit and Interfacial Area
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Verified HETP of Packed Columns using 25 and 50mm Raschig Rings
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Verified Interfacial Area given Height of Transfer Unit and Mass Transfer Coefficient
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Verified Interfacial Area of Packing Given Performance of Column and Gas Flowrate
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Verified Liquid Mass Film Coefficient in Packed Columns
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Verified Overall Gas Mass Transfer Coefficient given Height of Transfer Unit
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Verified Performance of Column for Known Value of Height of Transfer Unit
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Verified Performance of Column Given Gas-Film Transfer Coefficient and Vapor Flowrate
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Verified Pressure Drop Correlation given Vapor Mass Flux and Packing Factor
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4 More Packed Column Designing Calculators
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Verified Force acting on Surface
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7 More Pressure and its Measurement Calculators
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Verified Membrane Water Diffusivity Based on Solution Diffusion Model
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Verified Water Flux Based on Solution Diffusion Model
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24 More Properties of Fluids 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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Verified Diameter of Bolt
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Verified Diameter of Hub
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Verified Length of Hub
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Verified Number of Bolts Given Diameter
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Verified Outside Diameter of Flange
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Verified Pitch Circle Diameter of Bolts
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Verified Thickness of Protective Circumferential Flange
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8 More Shaft Couplings Calculators
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Created Projected Area of Solid Body
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Verified Settling Velocity of Group of Particles
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1 More Size Separation Calculators
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Verified Area between Bearing Plate and Concrete Foundation using Compressive Stress
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Verified Area using Minimum Stress
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Verified Circumferential Length of Bearing Plate given Maximum Bending Moment
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Verified Total Weight of Vessel given Maximum Compressive Stress
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3 More Skirt Supports Calculators
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Verified Effectiveness Factor at First Order
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Verified Initial Reactant Concentration for Rxn Containing Batch of Catalysts and Batch of Gas at 1st Order
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Verified Mass Transfer Coefficient of Fluid passing through Single Particle
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Verified Rate Constant for Mixed Flow Reactor with Weight of Catalyst
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Verified Rate of Reaction in Mixed Flow Reactor Containing Catalyst
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Verified Thiele Modulus
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4 More Solid Catalyzed Reactions Calculators
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Created Surface Shape Factor
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4 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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Verified Equilibrium Conversion of Reaction at Final Temperature
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Verified Equilibrium Conversion of Reaction at Initial Temperature
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Verified Initial Temperature for Equilibrium Conversion
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6 More Temperature and Pressure Effects Calculators
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Verified Rate Constant of Phase between Cloud-Wake and Emulsion
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Verified Rise Velocity of Bubble
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Verified Rise Velocity of Bubble in Bubbling Bed
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Verified Terminal Velocity of Fluids for Irregular Shaped Particles
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6 More Various Fluidized Reactors Calculators
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Washing (21)
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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