Calculators Created by Vaibhav Mishra

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 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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24 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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Verified Bundle Diameter given Number of Tubes in Centre Row and Pitch

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5 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 to 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 and 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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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