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Calculators Created by Vaibhav Mishra
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.
Adiabatic Saturation Temperature and Wet Bulb Temperature
(13)
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
Basic Formulas
(1)
Verified
Discharge Rate of Liquid from Orifice in Tank
Go
8 More Basic Formulas Calculators
Go
Basic Formulas
(2)
Created
Specific Surface Area of Mixture
Go
Created
Total Surface Area of Particle using Spericity
Go
7 More Basic Formulas Calculators
Go
Basic Formulas of Heat Exchanger Designs
(25)
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
Basics of Heat Transfer
(1)
Created
Logarithmic Mean Area of Cylinder
Go
16 More Basics of Heat Transfer Calculators
Go
Basics of Humidification Process
(11)
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
Basics of Membrane Separation Processes
(14)
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
Basics of Petrochemicals
(2)
Verified
Diesel Index
Go
Verified
Melt Flow Index
Go
7 More Basics of Petrochemicals Calculators
Go
Bundle Diameter in Heat Exchanger
(7)
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
Continuous Distillation
(11)
Created
Boil-Up Ratio
Go
Created
Bottom Product based on Boil-up Ratio
Go
Created
Distillate Flowrate based on External Reflux Ratio
Go
Created
Distillate Flowrate based on Internal Reflux Ratio
Go
Created
External Reflux Ratio
Go
Created
Feed Q-Value in Distillation Column
Go
Created
Internal Liquid Reflux Flowrate based on Internal Reflux Ratio
Go
Created
Internal Reflux Ratio
Go
Created
Liquid Reflux Flowrate based on External Reflux Ratio
Go
Created
Minimum Number of Distillation Stages by Fenske's Equation
Go
Created
Vapor Reflux based on Boil-Up Ratio
Go
2 More Continuous Distillation Calculators
Go
Cost Estimation
(4)
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
Counter Current Continuous Leaching for Constant Overflow (Pure Solvent)
(25)
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
Crystallization
(17)
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
Deactivating Catalysts
(9)
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
Depreciation
(8)
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
Design of Key
(2)
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
Design of Pressure Vessel Subjected to Internal Pressure
(4)
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
Diffusivity Measurement and Prediction
(5)
Created
Chapman Enskog Equation for Gas Phase Diffusivity
Go
Created
Diffusivity by Stefan Tube Method
Go
Created
Diffusivity by Twin Bulb Method
Go
Created
Fuller-Schettler-Giddings for Binary Gas Phase Diffusivity
Go
Created
Wilke Chang Equation for Liquid Phase Diffusivity
Go
Dispersion Model
(4)
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
Distillation Tower Design
(27)
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
Distribution Coefficient, Selectivity and Mass Ratio
(12)
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
Drying from Critical to Final Moisture
(9)
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
Drying from Initial to Critical Moisture
(11)
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
Drying from Initial to Final Moisture
(11)
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
Drying from Initial to Final Moisture
(9)
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
Drying Time
(3)
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
Earliness of Mixing,Segregation,RTD
(5)
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
Equilibrium Stage Calculations for Immiscible (Pure) Solvent and Carrier Liquid
(5)
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
Equimolar Counter Diffusion
(1)
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
Filtration
(4)
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
First Order followed by Zero Order Reaction
(1)
Created
Maximum Intermediate Concentration in First Order followed by Zero Order Reaction
Go
9 More First Order followed by Zero Order Reaction Calculators
Go
Fluidisation
(4)
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
Formulas on Size Reduction Laws
(7)
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
G to L Reactions on Solid Catalysts
(8)
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
Gas Absorption
(10)
Created
Absorption Factor
Go
Created
Absorption Factor given Stripping Factor
Go
Created
Gas Flowrate for Absorption Column on Solute Free Basis
Go
Created
Liquid Flowrate for Absorption Column on Solute Free basis
Go
Created
Maximum Gas Rate for Absorption Column
Go
Created
Minimum Liquid Rate for Absorption Column
Go
Created
Minimum Operating Line Slope for Absorption Column
Go
Created
Number of Absorption Stages by Kremser Equation
Go
Created
Number of Stages for Absorption Factor Equal to 1
Go
Created
Operating Line Slope for Absorption Column
Go
Gas Absorption and Stripping
(11)
Created
Corrected Murphree Efficiency Percentage for Liquid Entrainment
Go
Created
Gas Flowrate on Solute Free Basis for Inlet Conditions by Mole Fraction
Go
Created
Gas Flowrate on Solute Free Basis for Inlet Conditions by Solute Free Mole Fraction
Go
Created
Liquid Flowrate on Solute Free Basis for Inlet Conditions by Solute Free Mole Fraction
Go
Created
Liquid Flowrate on Solute Free Basis for Inlet Conditions using Mole Fraction
Go
Created
Murphree Efficiency of Absorption Operation Based on Point Efficiency for Plug Flow
Go
Created
Murphree Tray Efficiency of Absorption Operation
Go
Created
Overall Tray Efficiency for Absorption Column given Murphree Efficiency
Go
Created
Point Efficiency of Absorption Operation
Go
Created
Solute Free Mole Fraction of Gas in Inlet based on Mole Fraction
Go
Created
Solute Free Mole Fraction of Liquid in Inlet based on Mole Fraction
Go
Heat Transfer Coefficient in Heat Exchangers
(10)
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
Important Formulas in Size Reduction Laws
(3)
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
Kremser's Equation for Liquid Liquid Extraction
(6)
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
Manometers
(2)
Verified
Membrane Water Concentration Based on Solution Diffusion Model
Go
Created
Vapor Pressure of Water using Saturation Humidity
Go
1 More Manometers Calculators
Go
Mass Transfer Theories
(20)
Created
Average Contact Time by Penetration Theory
Go
Created
Average Mass Transfer Coefficient by Penetration Theory
Go
Created
Diffusivity by Average Contact Time in Penetration Theory
Go
Created
Diffusivity by Film Theory
Go
Created
Diffusivity by Instanataneous Contact Time in Penetration Theory
Go
Created
Diffusivity by Surface Renewal Theory
Go
Created
Film Thickness by Film Theory
Go
Created
Fractional Resistance Offered by Gas Phase
Go
Created
Fractional Resistance Offered by Liquid Phase
Go
Created
Gas Phase Mass Transfer Coefficient by Two Film Theory
Go
Created
Gas Phase Mass Transfer Coefficient using Fractional Resistance by Gas Phase
Go
Created
Instantaneous Contact Time by Penetration Theory
Go
Created
Instantaneous Mass Transfer Coefficient by Penetration Theory
Go
Created
Liquid Phase Mass Transfer Coefficient by Two Film Theory
Go
Created
Liquid Phase Mass Transfer Coefficient using Fractional Resistance by Liquid Phase
Go
Created
Mass Transfer Coefficient by Film Theory
Go
Created
Mass Transfer Coefficient by Surface Renewal Theory
Go
Created
Overall Gas Phase Mass Transfer Coefficient using Fractional Resistance by Gas Phase
Go
Created
Overall Liquid Phase Mass Transfer Coefficient using Fractional Resistance by Liquid Phase
Go
Created
Surface Renewal Rate by Surface Renewal Theory
Go
Material Balance
(14)
Created
Mole Fraction of MVC in Distillate from Overall and Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Distillate from Overall Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Feed from Overall and Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Feed from Overall Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Residue from Overall and Component Material Balance in Distillation
Go
Created
Mole Fraction of MVC in Residue from Overall Component Material Balance in Distillation
Go
Created
Total Distillate Flowrate of Distillation Column from Overall and Component Material Balance
Go
Created
Total Distillate Flowrate of Distillation Column from Overall Component Material Balance
Go
Created
Total Distillate Flowrate of Distillation Column from Overall Material Balance
Go
Created
Total Feed Flowrate of Distillation Column from Overall Component Material Balance
Go
Created
Total Feed Flowrate of Distillation Column from Overall Material Balance
Go
Created
Total Residue Flowrate of Distillation Column from Overall and Component Material Balance
Go
Created
Total Residue Flowrate of Distillation Column from Overall Component Material Balance
Go
Created
Total Residue Flowrate of Distillation Column from Overall Material Balance
Go
Mechanical Separation
(2)
Created
Combined Overall Efficiency of Screen
Go
Created
Screen Effectiveness based on Oversize Material from Overall Efficiency
Go
10 More Mechanical Separation Calculators
Go
Membrane Characteristics
(9)
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
Moisture Content
(10)
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
Operation
(6)
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
Packed Column Designing
(12)
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
Pressure and its Measurement
(1)
Verified
Force acting on Surface
Go
7 More Pressure and its Measurement Calculators
Go
Properties of Fluids
(2)
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
Ratio of Moisture Content
(18)
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
Relative Volatility and Vaporization Ratio
(7)
Created
Equilibrium Vaporization Ratio for Less Volatile Component
Go
Created
Equilibrium Vaporization Ratio for More Volatile Component
Go
Created
Mole Fraction of LVC in Liquid using Equilibrium Vaporization Ratio
Go
Created
Mole Fraction of LVC in Vapor using Equilibrium Vaporization Ratio
Go
Created
Mole Fraction of MVC in Liquid using Equilibrium Vaporization Ratio
Go
Created
Mole Fraction of MVC in Vapor using Equilibrium Vaporization Ratio
Go
Created
Relative Volatility using Equilibrium Vaporization Ratio
Go
3 More Relative Volatility and Vaporization Ratio Calculators
Go
Shaft Couplings
(7)
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
Size Separation
(2)
Created
Projected Area of Solid Body
Go
Verified
Settling Velocity of Group of Particles
Go
1 More Size Separation Calculators
Go
Skirt Supports
(4)
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
Solid Catalyzed Reactions
(6)
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
Sphericity of Particles
(1)
Created
Surface Shape Factor
Go
4 More Sphericity of Particles Calculators
Go
Steady State Diffusion
(1)
Created
Log Mean Mole Fraction of B
Go
8 More Steady State Diffusion Calculators
Go
Steam Distillation
(5)
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
Stripping
(3)
Created
Number of Stripping Stages by Kremser Equation
Go
Created
Stripping Factor
Go
Created
Stripping Factor given Absorption Factor
Go
Temperature and Pressure Effects
(3)
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
Various Fluidized Reactors
(4)
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
Weight of Moisture
(10)
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
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