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
Go
Created Air Humidity at Wet Bulb Temperature based on Heat and Mass Transfer Rates
Go
Created Air Inlet Temperature based on Adiabatic Saturation Temperature
Go
Created Ambient Air Humidity based on Wet Bulb Temperature
Go
Created Ambient Air Temperature based on Wet Bulb Temperature
Go
Created Heat Transfer Coefficient based on Wet Bulb Temperature
Go
Created Humid Heat of Air based on Adiabatic Saturation Temperature
Go
Created Inlet Air Humidity based on Adiabatic Saturation Temperature
Go
Created Latent Heat of Air based on Adiabatic Saturation Temperature
Go
Created Latent Heat of Air based on Wet Bulb Temperature
Go
Created Mass Transfer Coefficient based on Wet Bulb Temperature
Go
Created Saturated Exit Air Humidity based on Adiabatic Saturation Temperature
Go
Created Wet Bulb Temperature
Go
Verified Discharge Rate of Liquid from Orifice in Tank
Go
8 More Basic Formulas Calculators
Go
Created Specific Surface Area of Mixture
Go
Created Total Surface Area of Particle using Spericity
Go
7 More Basic Formulas Calculators
Go
Verified Allowable Length of Tube given Temperature Difference and Thermal Expansion of Tubes
Go
Verified Baffle Spacing given Tube Length and Number of Baffles
Go
Verified Channel Velocity of Fluid given Path Length and Plate Pressure Drop
Go
Verified Heat Duty of Exchanger given Core Volume of Exchanger for Air Separation
Go
Verified Heat Duty of Exchanger given Core Volume of Exchanger for Hydrocarbon Separation
Go
Verified Log Mean Temperature Difference in Plate Heat Exchanger Given Fluid Temperature and NTU
Go
Verified Number of Tubes in Eight Pass Square Pitch given Bundle Diameter
Go
Verified Number of Tubes in Eight Pass Triangular Pitch given Bundle Diameter
Go
Verified Number of Tubes in Four Pass Square Pitch given Bundle Diameter
Go
Verified Number of Tubes in Four Pass Triangular Pitch given Bundle Diameter
Go
Verified Number of Tubes in One Pass Square Pitch given Bundle Diameter
Go
Verified Number of Tubes in One Pass Triangular Pitch given Bundle Diameter
Go
Verified Number of Tubes in Six Pass Square Pitch given Bundle Diameter
Go
Verified Number of Tubes in Six Pass Triangular Pitch given Bundle Diameter
Go
Verified Number of Tubes in Two Pass Square Pitch given Bundle Diameter
Go
Verified Number of Tubes in Two Pass Triangular Pitch given Bundle Diameter
Go
Verified Outlet Temperature of Fluid in Plate Heat Exchanger given NTU and Log Mean Temperature Difference
Go
Verified Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop
Go
Verified Pressure Drop in Plate Type Heat Exchanger
Go
Verified Shell Diameter of Heat Exchanger Given Clearance and Bundle Diameter
Go
Verified Temperature Difference Achieved given Thermal Expansion and Length of Tubes in Heat Exchanger
Go
Verified Tube Side Mass Flowrate Given Pumping Power and Tube Side Pressure Drop
Go
Verified Tube Side Mass Flowrate of Liquid Given Number of Tubes and Fluid Velocity
Go
Verified Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid
Go
Verified Tube Side Velocity of Fluid Given Mass Flowrate and Number of Tubes
Go
24 More Basic Formulas of Heat Exchanger Designs Calculators
Go
Created Logarithmic Mean Area of Cylinder
Go
16 More Basics of Heat Transfer Calculators
Go
Created Absolute Humidity based on Humid Heat
Go
Created Absolute Humidity based on Humid Volume and Temperature
Go
Created Absolute Humidity based on Percentage and Saturation Humidity
Go
Created Humid Volume based on Absolute Humidity and Temperature
Go
Created Molal Humidity based on Absolute Humidity
Go
Created Moles of Air based on Molal Humidity
Go
Created Moles of Water Vapour based on Molal Humidity
Go
Created Saturation Humidity based on Percentage and Absolute Humidity
Go
Created Temperature based on Absolute Humidity and Humid Volume
Go
Created Weight of Air based on Absolute Humidity
Go
Created Weight of Water Vapour based on Absolute Humidity
Go
8 More Basics of Humidification Process Calculators
Go
Verified Applied Pressure Driving Force Based on Permeability of Membrane
Go
Verified Concentration of Mass at Membrane Surface
Go
Verified Hagen Poiseuille Based Flux for Membrane Separation
Go
Verified Liquid Flow through Pore Based On Poiseuilles Law
Go
Verified Liquid Viscosity based on Membrane Resistance
Go
Verified Liquid Viscosity based on Poiseuille's Law
Go
Verified Membrane Flux Based on Resistance
Go
Verified Membrane Flux Based on Water Permeability
Go
Verified Partial Molar Volume of Water based on Solution Diffusion Model
Go
Verified Pressure Difference across Pore based on Poiseuille's Law
Go
Verified Resistance to flow in Membranes
Go
Verified Time of Dialysis using Hollow Fiber Haemodialyser
Go
Verified Water Permeability based on Initial flux
Go
Verified Water Permeability through Membrane
Go
2 More Basics of Membrane Separation Processes Calculators
Go
Verified Diesel Index
Go
Verified Melt Flow Index
Go
7 More Basics of Petrochemicals Calculators
Go
Verified Bundle Diameter for Eight Tube Pass Square Pitch in Heat Exchanger
Go
Verified Bundle Diameter for Eight Tube Pass Triangular Pitch in Heat Exchanger
Go
Verified Bundle Diameter for Four Tube Pass Square Pitch in Heat Exchanger
Go
Verified Bundle Diameter for One Tube Pass Square Pitch in Heat Exchanger
Go
Verified Bundle Diameter for Six Tube Pass Square Pitch in Heat Exchanger
Go
Verified Bundle Diameter for Two Tube Pass Square Pitch in Heat Exchanger
Go
Verified Bundle Diameter given Number of Tubes in Centre Row and Pitch
Go
5 More Bundle Diameter in Heat Exchanger Calculators
Go
Created Boil-Up Ratio
Go
Created Bottom Product based on Boil-up Ratio
Go
Created Distillate Flowrate based on External Reflux Ratio
Go
Created Distillate Flowrate based on Internal Reflux Ratio
Go
Created External Reflux Ratio
Go
Created Feed Q-Value in Distillation Column
Go
Created Internal Liquid Reflux Flowrate based on Internal Reflux Ratio
Go
Created Internal Reflux Ratio
Go
Created Liquid Reflux Flowrate based on External Reflux Ratio
Go
Created Minimum Number of Distillation Stages by Fenske's Equation
Go
Created Vapor Reflux based on Boil-Up Ratio
Go
2 More Continuous Distillation Calculators
Go
Verified Fixed Capital Investment
Go
Verified Fixed Cost at Breakeven Point
Go
Verified Total Production Cost Considering Fixed Cost and Variable Cost
Go
Verified Working Capital Investment
Go
7 More Cost Estimation Calculators
Go
Created Fractional Solute Discharge based on Ratio of Overflow to Underflow
Go
Created Fractional Solute Discharge based on Recovery of Solute
Go
Created Fractional Solute Discharge Ratio based on Solute Underflow
Go
Created Number of Equilibirum Leaching Stages based on Fractional Solute Discharge
Go
Created Number of Equilibirum Leaching Stages based on Solute Underflow
Go
Created Number of Equilibrium Leaching Stages based on Recovery of Solute
Go
Created Ratio of Solute Discharged in Underflow to Overflow
Go
Created Ratio of Solution Discharged in Overflow to Underflow
Go
Created Ratio of Solvent Discharged in Underflow to Overflow
Go
Created Recovery of Solute based on Fractional Solute Discharge
Go
Created Recovery of Solute based on Solute Underflow
Go
Created Solute Discharged in Overflow based on Ratio of Overflow to Underflow
Go
Created Solute Discharged in Overflow based on Ratio of Overflow to Underflow and Solution Discharged
Go
Created Solute Discharged in Underflow based on Ratio of Overflow to Underflow
Go
Created Solute Discharged in Underflow based on Ratio of Overflow to Underflow and Solution Discharged
Go
Created Solute Underflow Entering Column based on Fractional Solute Discharge
Go
Created Solute Underflow Entering Column based on Ratio of Overflow to Underflow
Go
Created Solute Underflow Entering Column based on Recovery of Solute
Go
Created Solute Underflow Leaving Column based on Fractional Solute Discharge
Go
Created Solute Underflow Leaving Column based on Ratio of Overflow to Underflow
Go
Created Solute Underflow Leaving Column based on Recovery of Solute
Go
Created Solution Discharged in Overflow based on Ratio of Overflow to Underflow
Go
Created Solution Discharged in Overflow based on Ratio of Overflow to Underflow and Solute Discharged
Go
Created Solution Discharged in Underflow based on Ratio of Overflow to Underflow
Go
Created Solution Discharged in Underflow based on Ratio of Overflow to Underflow and Solute Discharged
Go
Verified Equilibrium Saturation Value given Relative Supersaturation and Degree of Saturation
Go
Verified Mass Flux Density given Mass Transfer Coefficient and Concentration Gradient
Go
Verified Mass Flux Density given Reaction Rate Constant and Order of Integration Reaction
Go
Verified Mass Transfer Coefficient given Mass Flux Density and Concentration Gradient
Go
Verified Nucleation Rate for given Number of Particles and Volume of Constant Supersaturation
Go
Verified Overall Excess Free Energy for Spherical Crystalline Body
Go
Verified Reaction Rate Constant in Crystallization given Mass Flux Density and Order of Reaction
Go
Verified Relative Supersaturation for given Supersaturation Ratio
Go
Verified Relative Supersaturation given Degree of Saturation and Equilibrium Saturation Value
Go
Verified Solubility Product given Activities of Species A and B
Go
Verified Solubility Product given Concentration of Species A and B
Go
Verified Supersaturation based on activities of Species A and B
Go
Verified Supersaturation based on Concentration of Species A and B along with Solubility Product
Go
Verified Supersaturation Ratio given Solution Concentration and Equilibrium Saturation Value
Go
Verified Supersaturation Time given Nucleation Rate and Supersaturation Volume
Go
Verified Supersaturation Volume given Nucleation Rate and Supersaturation Time
Go
Verified Suspension Density given Solid Density and Volumetric Holdup
Go
7 More Crystallization Calculators
Go
Verified Activity of Catalyst
Go
Verified Deactivation rate for Batch Solids and Mixed Changing Flow of Fluids
Go
Verified Deactivation Rate for Batch Solids and Plug Changing Flow of Fluids
Go
Verified Deactivation rate for Batch Solids and Plug Constant Flow of Fluids
Go
Verified Deactivation Rate in Batch Solids and Mixed Constant Flow of Fluids
Go
Verified Initial Reactant Concentration of Reactant for No Pore Resistance in Catalyst Deactivation
Go
Verified Rate Constant based on Weight of Catalyst in Batch Solids and Mixed Constant Flow of Fluids
Go
Verified Volume of Reactor for Batch Solids and Batch Fluids
Go
Verified Weight of Catalyst in Batch Solids and Batch Fluids
Go
6 More Deactivating Catalysts Calculators
Go
Verified Annual Depreciation by Straight-Line Method
Go
Verified Asset Value after 'a' Years
Go
Verified Asset Value using Declining Balance Method
Go
Verified Book Value of Process Equipment at any Time during Service Life
Go
Verified Depletion Cost
Go
Verified Depreciation by Sum of Year Digit Method
Go
Verified Fixed Percentage Factor using Matheson Formula
Go
Verified Replacement Value by Sinking Fund Method
Go
Verified Length of Key based on Crushing Stress in Key
Go
Verified Thickness of Key based on Crushing Stress
Go
6 More Design of Key Calculators
Go
Verified Internal Pressure of Cylindrical Vessel given Hoop Stress
Go
Verified Internal Presure of Vessel given Longitudinal Stress
Go
Verified Wall Thickness of Cylindrical Shell Given Hoop Stress
Go
Verified Wall Thickness of Pressure Vessel given Longitudinal Stress
Go
13 More Design of Pressure Vessel Subjected to Internal Pressure Calculators
Go
Created Chapman Enskog Equation for Gas Phase Diffusivity
Go
Created Diffusivity by Stefan Tube Method
Go
Created Diffusivity by Twin Bulb Method
Go
Created Fuller-Schettler-Giddings for Binary Gas Phase Diffusivity
Go
Created Wilke Chang Equation for Liquid Phase Diffusivity
Go
Verified Dispersion Coefficient based on Variance of Spread of Tracer at Small Extents of Dispersion
Go
Verified Length of Spread based on Variance of Spread of Tracer for Small Extents of Dispersion
Go
Verified Mean Residence Time where Dispersion Number is less than 0.01
Go
Verified Standard Deviation of Tracer based on Mean Residence Time for Large Deviations of Dispersion
Go
5 More Dispersion Model Calculators
Go
Verified Active Area Given Total Area and Fractional Downcomer Area
Go
Verified Clearance Area under Downcomer given Weir Length and Apron Height
Go
Verified Column Diameter given Maximum Vapor Rate and Maximum Vapor Velocity
Go
Verified Downcomer Liquid Load in Trays
Go
Verified Downcomer Residence Time in Distillation Column
Go
Verified Dry Plate Pressure Drop in Distillation Column Design
Go
Verified External Reflux Ratio given Internal Reflux Ratio
Go
Verified Flooding Velocity for given Flooding Constant
Go
Verified Flooding Velocity in Distillation Column Design
Go
Verified Head Loss in Downcomer of Tray Tower
Go
Verified Height of Liquid Crest over Weir
Go
Verified Length of Weir given Clearance Area and Apron Height of Tray
Go
Verified Liquid Flowrate in Rectifying Section for given Quality of Feed
Go
Verified Liquid Flowrate over Tray for given Dowcomer Liquid Load
Go
Verified Liquid Vapor Flow Factor in Distillation Column Design
Go
Verified Maximum Allowable Vapor Velocity given Plate Spacing and Fluid Densities
Go
Verified Quality of Feed based on Enthalpy of Feed and Latent Heat of Vaporization
Go
Verified Quality of Feed Based on Liquid Flowrates and Feed Flowrate
Go
Verified Rectifying Section Flowrate of Liquid for given Quality of Feed
Go
Verified Rectifying Section Flowrate of Vapor for given Quality of Feed
Go
Verified Residual Head Loss in Pressure in Distillation Column
Go
Verified Souders and Brown Flooding Constant
Go
Verified Stripping Section Flowrate of Liquid for given Quality of Feed
Go
Verified Stripping Section Flowrate of Vapor for given Quality of Feed
Go
Verified Vapor Flowrate in Rectifying Section for given Quality of Feed
Go
Verified Weep Fraction of Tray
Go
Verified Weep Point Velocity in Distillation Column Design
Go
14 More Distillation Tower Design Calculators
Go
Created Distribution Coefficient of Carrier Liquid from Activity Coefficients
Go
Created Distribution Coefficient of Carrier Liquid from Mass Fraction
Go
Created Distribution Coefficient of Solute from Activity Coefficient
Go
Created Distribution Coefficient of Solute from Mass Fractions
Go
Created Mass Ratio of Solute in Extract Phase
Go
Created Mass Ratio of Solute in Raffinate Phase
Go
Created Mass Ratio of Solvent in Extract Phase
Go
Created Mass Ratio of Solvent in Raffinate Phase
Go
Created Recovery of Solute in Liquid-Liquid Extraction
Go
Created Selectivity of Solute based on Distribution Coefficients
Go
Created Selectvity of Solute based on Activity Coefficients
Go
Created Selectvity of Solute based on Mole Fractions
Go
Created Dry Weight of Solid based on Critical to Final Moisture Content for Falling Rate Period
Go
Created Drying Surface Area based on Critical to Final Moisture Content for Falling Rate Period
Go
Created Drying Surface Area based on Critical to Final Weight of Moisture for Falling Rate Period
Go
Created Falling Rate Drying Time from Critical to Final Moisture
Go
Created Falling Rate Drying Time from Critical to Final Weight of Moisture
Go
Created Final Moisture Content based on Critical to Final Moisture Content for Falling Rate Period
Go
Created Final Weight of Moisture based on Critical to Final Weight of Moisture for Falling Rate Period
Go
Created Rate of Constant Drying Period based on Critical to Final Moisture Content for Falling Rate Period
Go
Created Rate of Constant Drying Period based on Critical to Final Weight of Moisture for Falling Rate Period
Go
Created Constant Drying Time from Initial to Critical Moisture Content
Go
Created Constant Drying Time from Initial to Critical Weight of Moisture
Go
Created Critical Moisture Content based on Initial Moisture Content for Constant Rate Period
Go
Created Critical Weight of Moisture based on Initial Weight of Moisture for Constant Rate Period
Go
Created Dry Weight of Solid from Initial to Critical Moisture Content for Constant Rate Period
Go
Created Drying Surface Area based on Initial to Critical Moisture Content for Constant Rate Period
Go
Created Drying Surface Area based on Initial to Critical Weight of Moisture for Constant Rate Period
Go
Created Initial Moisture Content based on Critical Moisture Content for Constant Rate Period
Go
Created Initial Weight of Moisture based on Critical Weight of Moisture for Constant Rate Period
Go
Created Rate of Constant Drying Period based on Critical Moisture Content
Go
Created Rate of Constant Drying Period based on Critical Weight of Moisture
Go
Created Constant Drying Time from Initial to Final Moisture Content
Go
Created Constant Drying Time from Initial to Final Weight of Moisture
Go
Created Dry Weight of Solid from Initial to Final Moisture Content for Constant Rate Period
Go
Created Drying Surface Area based on Initial to Final Moisture Content for Constant Rate Period
Go
Created Drying Surface Area based on Initial to Final Weight of Moisture for Constant Rate Period
Go
Created Final Moisture Content based on Initial Moisture Content for Constant Rate Period
Go
Created Final Weight of Moisture based on Initial Weight of Moisture for Constant Rate Period
Go
Created Initial Moisture Content based on Final Moisture Content for Constant Rate Period
Go
Created Initial Weight of Moisture based on Final Weight of Moisture for Constant Rate Period
Go
Created Rate of Constant Drying Period based on Final Moisture Content
Go
Created Rate of Constant Drying Period based on Final Weight of Moisture
Go
Created Dry Weight of Solid based on Initial to Final Moisture Content for Falling Rate Period
Go
Created Drying Surface Area based on Initial to Final Moisture Content for Falling Rate Period
Go
Created Drying Surface Area based on Initial to Final Weight of Moisture for Falling Rate Period
Go
Created Falling Rate Drying Time from Initial to Final Moisture
Go
Created Falling Rate Drying Time from Initial to Final Weight of Moisture
Go
Created Final Moisture Content based on Initial to Final Moisture Content for Falling Rate Period
Go
Created Final Weight of Moisture based on Initial to Final Weight of Moisture for Falling Rate Period
Go
Created Rate of Constant Drying Period based on Initial to Final Moisture Content for Falling Rate Period
Go
Created Rate of Constant Drying Period based on Initial to Final Weight of Moisture for Falling Rate Period
Go
Created Constant Drying Time based on Total Drying Time and Falling Drying Time
Go
Created Falling Drying Time based on Constant Drying Time and Total Drying Time
Go
Created Total Drying Time based on Constant Drying Time and Falling Drying Time
Go
Verified Initial Reactant Concentration of Microfluid treated in Mixed Flow Reactor
Go
Verified Life of Element in Fluid
Go
Verified Reactant Concentration of Macrofluid in Mixed Flow Reactor at First Order
Go
Verified Reactant Concentration of Macrofluid in Mixed Flow Reactor at Zero Order
Go
Verified Reactant Concentration of Microfluid and Macrofluid in Plug Flow Reactor at Second Order
Go
4 More Earliness of Mixing,Segregation,RTD Calculators
Go
Created Feed Solute Concentration for N-number of Ideal Stage Extraction
Go
Created Feed Solute Concentration for Single Ideal Stage Extraction
Go
Created Number of Ideal Equilibrium Extraction Stages
Go
Created Raffinate Phase Solute Concentration for N Number of Ideal Stage Extraction
Go
Created Raffinate Phase Solute Concentration for Single Ideal Stage Extraction
Go
Created Molar Flux of Diffusing Component A for Equimolar Diffusion with B based on Concentration of A
Go
2 More Equimolar Counter Diffusion Calculators
Go
Created Equivalent Diameter using Reynolds Number
Go
Created Fraction of Cycle Time used for Cake Formation
Go
Created Time Required for Cake Formation
Go
Verified Total Cycle Time Required for Cake Formation
Go
Created Maximum Intermediate Concentration in First Order followed by Zero Order Reaction
Go
9 More First Order followed by Zero Order Reaction Calculators
Go
Verified Dynamic Viscosity based on Kozeny Carman Equation
Go
Created Pressure Gradient using Kozeny Carman Equation
Go
Verified Total Volume of Bed Based on Porosity
Go
Verified Volume of Voids in Bed Based on Porosity
Go
1 More Fluidisation Calculators
Go
Created Area of Product given Crushing Efficiency
Go
Verified Feed Rate to Machine for Size Reduction of Particles
Go
Created Maximum Diameter of Particle Nipped by Rolls
Go
Verified Power Consumption by Mill while Crushing
Go
Verified Power Required by Machine for Size Reduction of Particles
Go
Created Radius of Crushing Rolls
Go
Created Work required for Reduction of Particles
Go
6 More Formulas on Size Reduction Laws Calculators
Go
Verified Concentration of Reactant B at Extreme A
Go
Verified Concentration of Reactant B in G/L Reactions
Go
Verified Henry's Law Constant
Go
Verified Inner Area of Particle
Go
Verified Liquid Holdup
Go
Verified Rate Equation of Reactant A in G/L Reactions
Go
Verified Rate Equation of Reactant B in G/L Reactions
Go
Verified Solid Loading
Go
5 More G to L Reactions on Solid Catalysts Calculators
Go
Created Absorption Factor
Go
Created Absorption Factor given Stripping Factor
Go
Created Gas Flowrate for Absorption Column on Solute Free Basis
Go
Created Liquid Flowrate for Absorption Column on Solute Free basis
Go
Created Maximum Gas Rate for Absorption Column
Go
Created Minimum Liquid Rate for Absorption Column
Go
Created Minimum Operating Line Slope for Absorption Column
Go
Created Number of Absorption Stages by Kremser Equation
Go
Created Number of Stages for Absorption Factor Equal to 1
Go
Created Operating Line Slope for Absorption Column
Go
Created Corrected Murphree Efficiency Percentage for Liquid Entrainment
Go
Created Gas Flowrate on Solute Free Basis for Inlet Conditions by Mole Fraction
Go
Created Gas Flowrate on Solute Free Basis for Inlet Conditions by Solute Free Mole Fraction
Go
Created Liquid Flowrate on Solute Free Basis for Inlet Conditions by Solute Free Mole Fraction
Go
Created Liquid Flowrate on Solute Free Basis for Inlet Conditions using Mole Fraction
Go
Created Murphree Efficiency of Absorption Operation Based on Point Efficiency for Plug Flow
Go
Created Murphree Tray Efficiency of Absorption Operation
Go
Created Overall Tray Efficiency for Absorption Column given Murphree Efficiency
Go
Created Point Efficiency of Absorption Operation
Go
Created Solute Free Mole Fraction of Gas in Inlet based on Mole Fraction
Go
Created Solute Free Mole Fraction of Liquid in Inlet based on Mole Fraction
Go
Verified Heat Transfer Coefficient with Tube Loading for Condensation Inside Vertical Tubes
Go
Verified Heat Transfer Coefficient with Tube Loading for Condensation Outside Horizontal Tubes
Go
Verified Heat Transfer Coefficient with Tube Loading for Condensation Outside Vertical Tubes
Go
Verified Horizontal Tube Loading for Outside Condensation
Go
Verified Length of Tubes in Horizontal Condenser given Tube Loading and Condensate Flowrate
Go
Verified Number of Tubes in Horizontal Condenser given Condensate Flowrate and Tube Loading
Go
Verified Reynolds Number for Condensate Film given Tube Loading
Go
Verified Vertical Tube Loading for Inside Condensation
Go
Verified Vertical Tube Loading for Outside Condensation
Go
Verified Vertical Tube Loading given Reynolds Number for Condensate Film
Go
9 More Heat Transfer Coefficient in Heat Exchangers Calculators
Go
Verified Feed Diameter based on Reduction Law
Go
Verified Power Consumption while Mill is Empty
Go
Verified Product Diameter Based on Reduction Ratio
Go
16 More Important Formulas in Size Reduction Laws Calculators
Go
Created Extraction Factor at Feed Point Slope of Equilibrium Curve
Go
Created Extraction Factor at Mean Slope of Equilibrium Curve
Go
Created Extraction Factor based on Raffinate Point Slope
Go
Created Geometric Mean of Equilibrium Line Slope
Go
Created Number of Extraction Stages by Kremser Equation
Go
Created Number of Stages for Extraction Factor equal to 1
Go
Verified Membrane Water Concentration Based on Solution Diffusion Model
Go
Created Vapor Pressure of Water using Saturation Humidity
Go
1 More Manometers Calculators
Go
Created Average Contact Time by Penetration Theory
Go
Created Average Mass Transfer Coefficient by Penetration Theory
Go
Created Diffusivity by Average Contact Time in Penetration Theory
Go
Created Diffusivity by Film Theory
Go
Created Diffusivity by Instanataneous Contact Time in Penetration Theory
Go
Created Diffusivity by Surface Renewal Theory
Go
Created Film Thickness by Film Theory
Go
Created Fractional Resistance Offered by Gas Phase
Go
Created Fractional Resistance Offered by Liquid Phase
Go
Created Gas Phase Mass Transfer Coefficient by Two Film Theory
Go
Created Gas Phase Mass Transfer Coefficient using Fractional Resistance by Gas Phase
Go
Created Instantaneous Contact Time by Penetration Theory
Go
Created Instantaneous Mass Transfer Coefficient by Penetration Theory
Go
Created Liquid Phase Mass Transfer Coefficient by Two Film Theory
Go
Created Liquid Phase Mass Transfer Coefficient using Fractional Resistance by Liquid Phase
Go
Created Mass Transfer Coefficient by Film Theory
Go
Created Mass Transfer Coefficient by Surface Renewal Theory
Go
Created Overall Gas Phase Mass Transfer Coefficient using Fractional Resistance by Gas Phase
Go
Created Overall Liquid Phase Mass Transfer Coefficient using Fractional Resistance by Liquid Phase
Go
Created Surface Renewal Rate by Surface Renewal Theory
Go
Created Mole Fraction of MVC in Distillate from Overall and Component Material Balance in Distillation
Go
Created Mole Fraction of MVC in Distillate from Overall Component Material Balance in Distillation
Go
Created Mole Fraction of MVC in Feed from Overall and Component Material Balance in Distillation
Go
Created Mole Fraction of MVC in Feed from Overall Component Material Balance in Distillation
Go
Created Mole Fraction of MVC in Residue from Overall and Component Material Balance in Distillation
Go
Created Mole Fraction of MVC in Residue from Overall Component Material Balance in Distillation
Go
Created Total Distillate Flowrate of Distillation Column from Overall and Component Material Balance
Go
Created Total Distillate Flowrate of Distillation Column from Overall Component Material Balance
Go
Created Total Distillate Flowrate of Distillation Column from Overall Material Balance
Go
Created Total Feed Flowrate of Distillation Column from Overall Component Material Balance
Go
Created Total Feed Flowrate of Distillation Column from Overall Material Balance
Go
Created Total Residue Flowrate of Distillation Column from Overall and Component Material Balance
Go
Created Total Residue Flowrate of Distillation Column from Overall Component Material Balance
Go
Created Total Residue Flowrate of Distillation Column from Overall Material Balance
Go
Created Combined Overall Efficiency of Screen
Go
Created Screen Effectiveness based on Oversize Material from Overall Efficiency
Go
10 More Mechanical Separation Calculators
Go
Verified Bulk Concentration of Membrane
Go
Verified Initial Flux of Membrane
Go
Verified Initial Membrane Volume
Go
Verified Membrane Pressure Drop
Go
Verified Membrane Pressure Drop Based On Solution Diffusion Model
Go
Verified Membrane Thickness
Go
Verified Membrane Thickness Based on Solution Diffusion Model
Go
Verified Osmotic Pressure Drop Based on Solution Diffusion Model
Go
Verified Pressure Driving Force in Membrane
Go
4 More Membrane Characteristics Calculators
Go
Created Bound Moisture Content based on Free and Equilibrium Moisture Content
Go
Created Bound Moisture Content based on Unbound Moisture Content
Go
Created Equilibrium Moisture Content based on Bound and Unbound Moisture Content
Go
Created Equilibrium Moisture Content based on Free Moisture Content
Go
Created Free Moisture Content based on Bound and Unbound Moisture Content
Go
Created Free Moisture Content based on Equilibrium Moisture Content
Go
Created Initial Moisture Content based on Bound and Unbound Moisture Content
Go
Created Initial Moisture Content based on Free and Equlibrium Moisture Content
Go
Created Unbound Moisture Content based on Bound Moisture Content
Go
Created Unbound Moisture Content based on Free and Equilibrium Moisture Content
Go
Created Area of Contact for Batch Leaching Operation
Go
Created Concentration of Saturated Solution in Contact with Solid in Batch Leaching
Go
Created Concentration of Solute in Bulk Solution at Time t for Batch Leaching
Go
Created Mass Transfer Coefficient for Batch Leaching
Go
Created Time of Batch Leaching Operation
Go
Created Volume of Leaching Solution in Batch Leaching
Go
Verified Effective Interfacial Area of Packing using Onda's Method
Go
Verified Gas Film Mass Transfer Coefficient given Column Performance and Interfacial Area
Go
Verified Gas Flowrate given Column Performance and Interfacial Area
Go
Verified Gas Molar Flux given Height of Transfer Unit and Interfacial Area
Go
Verified HETP of Packed Columns using 25 and 50mm Raschig Rings
Go
Verified Interfacial Area given Height of Transfer Unit and Mass Transfer Coefficient
Go
Verified Interfacial Area of Packing Given Performance of Column and Gas Flowrate
Go
Verified Liquid Mass Film Coefficient in Packed Columns
Go
Verified Overall Gas Mass Transfer Coefficient given Height of Transfer Unit
Go
Verified Performance of Column for Known Value of Height of Transfer Unit
Go
Verified Performance of Column Given Gas-Film Transfer Coefficient and Vapor Flowrate
Go
Verified Pressure Drop Correlation given Vapor Mass Flux and Packing Factor
Go
4 More Packed Column Designing Calculators
Go
Verified Force acting on Surface
Go
7 More Pressure and its Measurement Calculators
Go
Verified Membrane Water Diffusivity Based on Solution Diffusion Model
Go
Verified Water Flux Based on Solution Diffusion Model
Go
24 More Properties of Fluids Calculators
Go
Created Bound Moisture Content based on Weight of Bound Moisture
Go
Created Critical Moisture Content based on Weight of Critical Moisture
Go
Created Dry Weight of Solid based on Bound Moisture Content
Go
Created Dry Weight of Solid based on Critical Moisture Content
Go
Created Dry Weight of Solid based on Equilibrium Moisture Content
Go
Created Dry Weight of Solid based on Free Moisture Content
Go
Created Dry Weight of Solid based on Initial Moisture Content
Go
Created Dry Weight of Solid based on Unbound Moisture Content
Go
Created Equilibrium Moisture Content based on Weight of Equilibrium Moisture
Go
Created Free Moisture Content based on Weight of Free Moisture
Go
Created Initial Moisture Content based on Weight of Initial Moisture
Go
Created Unbound Moisture Content based on Weight of Unbound Moisture
Go
Created Weight of Bound Moisture based on Bound Moisture Content
Go
Created Weight of Critical Moisture based on Critical Moisture Content
Go
Created Weight of Equilibrium Moisture based on Equilibrium Moisture Content
Go
Created Weight of Free Moisture based on Free Moisture Content
Go
Created Weight of Initial Moisture based on Initial Moisture Content
Go
Created Weight of Unbound Moisture based on Unbound Moisture Content
Go
Created Equilibrium Vaporization Ratio for Less Volatile Component
Go
Created Equilibrium Vaporization Ratio for More Volatile Component
Go
Created Mole Fraction of LVC in Liquid using Equilibrium Vaporization Ratio
Go
Created Mole Fraction of LVC in Vapor using Equilibrium Vaporization Ratio
Go
Created Mole Fraction of MVC in Liquid using Equilibrium Vaporization Ratio
Go
Created Mole Fraction of MVC in Vapor using Equilibrium Vaporization Ratio
Go
Created Relative Volatility using Equilibrium Vaporization Ratio
Go
3 More Relative Volatility and Vaporization Ratio Calculators
Go
Verified Diameter of Bolt
Go
Verified Diameter of Hub
Go
Verified Length of Hub
Go
Verified Number of Bolts Given Diameter
Go
Verified Outside Diameter of Flange
Go
Verified Pitch Circle Diameter of Bolts
Go
Verified Thickness of Protective Circumferential Flange
Go
8 More Shaft Couplings Calculators
Go
Created Projected Area of Solid Body
Go
Verified Settling Velocity of Group of Particles
Go
1 More Size Separation Calculators
Go
Verified Area between Bearing Plate and Concrete Foundation using Compressive Stress
Go
Verified Area using Minimum Stress
Go
Verified Circumferential Length of Bearing Plate given Maximum Bending Moment
Go
Verified Total Weight of Vessel given Maximum Compressive Stress
Go
3 More Skirt Supports Calculators
Go
Verified Effectiveness Factor at First Order
Go
Verified Initial Reactant Concentration for Rxn Containing Batch of Catalysts and Batch of Gas at 1st Order
Go
Verified Mass Transfer Coefficient of Fluid passing through Single Particle
Go
Verified Rate Constant for Mixed Flow Reactor with Weight of Catalyst
Go
Verified Rate of Reaction in Mixed Flow Reactor Containing Catalyst
Go
Verified Thiele Modulus
Go
4 More Solid Catalyzed Reactions Calculators
Go
Created Surface Shape Factor
Go
4 More Sphericity of Particles Calculators
Go
Created Log Mean Mole Fraction of B
Go
8 More Steady State Diffusion Calculators
Go
Created Moles of Volatile component Volatilized by Steam with Trace amounts of Non-Volatiles
Go
Created Moles of Volatile component Volatilized by Steam with Trace amounts of Non-Volatiles at Equilibrium
Go
Created Moles of Volatile component Volatilized from mixture of Non-Volatiles by Steam
Go
Created Moles of Volatile component Volatilized from mixture of Non-Volatiles by Steam at Equilibrium
Go
Created Total Steam Required to Vaporize Volatile Component
Go
Created Number of Stripping Stages by Kremser Equation
Go
Created Stripping Factor
Go
Created Stripping Factor given Absorption Factor
Go
Verified Equilibrium Conversion of Reaction at Final Temperature
Go
Verified Equilibrium Conversion of Reaction at Initial Temperature
Go
Verified Initial Temperature for Equilibrium Conversion
Go
6 More Temperature and Pressure Effects Calculators
Go
Verified Rate Constant of Phase between Cloud-Wake and Emulsion
Go
Verified Rise Velocity of Bubble
Go
Verified Rise Velocity of Bubble in Bubbling Bed
Go
Verified Terminal Velocity of Fluids for Irregular Shaped Particles
Go
6 More Various Fluidized Reactors Calculators
Go
Washing (21)
Created Amount of Solvent Decanted
Go
Created Amount of Solvent Remaining
Go
Created Beta Value based on Number of Stages and Fraction of Solute
Go
Created Beta Value based on Original Weight of Solute
Go
Created Beta Value based on Ratio of Solvent
Go
Created Fraction of Solute as Ratio of Solute
Go
Created Fraction of Solute Remaining based on Beta Value
Go
Created Fraction of Solute remaining based on Solvent Decanted
Go
Created Number of Stages based on Original Weight of Solute
Go
Created Number of Stages based on Solvent Decanted
Go
Created Number of Stages for Leaching based on Fraction Solute Retained and Beta Value
Go
Created Original Weight of Solute based on Number of Stages and Amount of Solvent Decanted
Go
Created Original Weight of Solute based on Number of Stages and Beta Value
Go
Created Original Weight of Solute in Solid before Washing
Go
Created Solvent Decanted based on Fraction of Solute remaining and Number of Stages
Go
Created Solvent Decanted based on Original Weight of Solute and Number of Stages
Go
Created Solvent Remaining based on Fraction of Solute remaining and Number of Stages
Go
Created Solvent Remaining based on Original Weight of Solute and Number of Stages
Go
Created Weight of Solute remaining based on Number of Stages and Amount of Solvent Decanted
Go
Created Weight of Solute remaining based on Number of Stages and Beta Value
Go
Created Weight of Solute remaining in Solid
Go
Created Bound Moisture Weight based on Free and Equilibrium Moisture Weight
Go
Created Bound Moisture Weight based on Unbound Moisture Weight
Go
Created Equilibrium Moisture Weight based on Bound and Unbound Moisture Weight
Go
Created Equilibrium Moisture Weight based on Free Moisture Weight
Go
Created Free Moisture Weight based on Bound and Unbound Moisture Weight
Go
Created Free Moisture Weight based on Equilibrium Moisture Weight
Go
Created Initial Moisture based on Free and Equlibrium Moisture Weight
Go
Created Initial Moisture Weight based on Bound and Unbound Moisture Weight
Go
Created Unbound Moisture Weight based on Bound Moisture Weight
Go
Created Unbound Moisture Weight based on Free and Equilibrium Moisture Weight
Go
Let Others Know
Facebook
Twitter
Reddit
LinkedIn
Email
WhatsApp
Copied!