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Calculators Created by Pavan Kumar
Pavan Kumar
Anurag Group of Institutions
(AGI)
,
Hyderabad
https://www.linkedin.com/in/v-r-s-c-pavan-kumar-madduri-607909224
113
Formulas Created
1
Formulas Verified
12
Across Categories
List of Calculators by Pavan Kumar
Following is a combined list of all the calculators that have been created and verified by Pavan Kumar. Pavan Kumar has created 113 and verified 1 calculators across 12 different categories till date.
Adiabatic Saturation Temperature and Wet Bulb Temperature
(1)
Verified
Saturated Exit Air Humidity based on Adiabatic Saturation Temperature
Go
12 More Adiabatic Saturation Temperature and Wet Bulb Temperature Calculators
Go
Basics of Non Ideal Flow
(10)
Created
Area under C-Pulse Curve
Go
Created
Exit Age Distribution based on Mean Residence Time
Go
Created
Exit Age Distribution Curve from C Pulse Curve
Go
Created
F Curve
Go
Created
Initial Concentration of Reactant in Plug Flow Reactant with Negligible Density Changes
Go
Created
Mean of C Pulse Curve
Go
Created
Rate Constant for Plug Flow Reactor using Space Time for Negligible Density Changes
Go
Created
Space Time for Plug Flow Reactor with Negligible Density Changes
Go
Created
Volume of Reactor based on Exit Age Distribution
Go
Created
Volumetric Flow Rate based on Mean Pulse Curve
Go
Convection Model for Laminar Flow
(9)
Created
Bodenstein Number
Go
Created
Concentration of Reactant for Chemical Conversions for Second Order in Laminar Flow Reactors
Go
Created
Dispersion using General Axis Expression
Go
Created
Dispersion using Taylor Expression Formula
Go
Created
F Curve for Laminar Flow in Pipes for Improper RTD
Go
Created
F Curve for Laminar Flow in Pipes for Proper RTD
Go
Created
Mean Residence Time for Improper RTD
Go
Created
Mean Residence Time for Proper RTD
Go
Created
Reactant Concentration for Chemical Conversions for Zero Order in Laminar Flow Reactors
Go
Deactivating Catalysts
(15)
Created
Activity of Catalyst
Go
Created
Deactivation rate for Batch Solids and Mixed Changing Flow of Fluids
Go
Created
Deactivation Rate for Batch Solids and Plug Changing Flow of Fluids
Go
Created
Deactivation rate for Batch Solids and Plug Constant Flow of Fluids
Go
Created
Deactivation Rate in Batch Solids and Mixed Constant Flow of Fluids
Go
Created
Initial Reactant Concentration of Reactant for No Pore Resistance in Catalyst Deactivation
Go
Created
Initial Reactant Concentration of Reactant for Strong Pore Resistance in Catalyst Deactivation
Go
Created
Rate Constant based on Weight of Catalyst in Batch Solids and Batch Fluids
Go
Created
Rate Constant based on Weight of Catalyst in Batch Solids and Mixed Changing Flow of Fluids
Go
Created
Rate Constant based on Weight of Catalyst in Batch Solids and Mixed Constant Flow of Fluids
Go
Created
Rate Constant based on Weight of Catalyst in Batch Solids and Plug Changing Flow of Fluids
Go
Created
Rate Constant based on Weight of Catalyst in Batch Solids and Plug Constant Flow of Fluids
Go
Created
Thiele Modulus for Deactivation
Go
Created
Volume of Reactor for Batch Solids and Batch Fluids
Go
Created
Weight of Catalyst in Batch Solids and Batch Fluids
Go
Dispersion Model
(9)
Created
Concentration using Dispersion where Dispersion Number less than 0.01
Go
Created
Dispersion Coefficient based on Variance of Spread of Tracer at Small Extents of Dispersion
Go
Created
Exit Age Distribution based on Dispersion Number
Go
Created
Length of Spread based on Variance of Spread of Tracer for Small Extents of Dispersion
Go
Created
Mean Residence Time where Dispersion Number is less than 0.01
Go
Created
Standard Deviation of Spread based on Mean Residence Time for Small Extents of Dispersion
Go
Created
Standard Deviation of Tracer based on Mean Residence Time for Large Deviations of Dispersion
Go
Created
Variance of Spread of Tracer for Small Extents of Dispersion
Go
Created
Velocity of Pulse based on Variance of Spread of Tracer
Go
Earliness of Mixing,Segregation,RTD
(9)
Created
Initial Reactant Concentration of Macrofluid in Mixed Flow Reactor at First Order
Go
Created
Initial Reactant Concentration of Microfluid in Mixed Flow Reactor at First Order
Go
Created
Initial Reactant Concentration of Microfluid in Mixed Flow Reactor at Zero Order
Go
Created
Initial Reactant Concentration of Microfluid treated in Mixed Flow Reactor
Go
Created
Life of Element in Fluid
Go
Created
Reactant Concentration of Macrofluid in Mixed Flow Reactor at First Order
Go
Created
Reactant Concentration of Macrofluid in Mixed Flow Reactor at Zero Order
Go
Created
Reactant Concentration of Microfluid and Macrofluid in Plug Flow Reactor at Second Order
Go
Created
Reactant Concentration of Microfluid treated in Mixed Flow Reactor
Go
Fluid-Fluid Reactions Kinetics
(10)
Created
Final Rate Expression for Straight Mass Transfer
Go
Created
Fraction of Gas in Fluid Fluid Kinetics
Go
Created
Fraction of Liquid in Fluid Kinetics
Go
Created
General Rate Equation of Mass Transfer
Go
Created
Interfacial Area of Contactor
Go
Created
Interfacial Area of Liquid in Contactor
Go
Created
Rate Equation of Reactant A for Straight Mass Transfer for Gas Film using Surface Area of Contactor
Go
Created
Rate Equation of Reactant A for Straight Mass Transfer for Gas Film using Volume of Contactor
Go
Created
Rate of Reactant A for Straight Mass Transfer for Liquid Film using Surface Area of Contactor
Go
Created
Rate of Reactant A for Straight Mass Transfer for Liquid Film using Volume of Contactor
Go
G/L Reactions on Solid Catalysts
(13)
Created
Concentration of Reactant B at Extreme A
Go
Created
Concentration of Reactant B in G/L Reactions
Go
Created
External Area of Particle
Go
Created
Henry's Law Constant
Go
Created
Inner Area of Particle
Go
Created
Liquid Holdup
Go
Created
Partial Pressure of Gaseous A at Extreme B
Go
Created
Partial Pressure of Gaseous A in G/L Reactions
Go
Created
Rate Equation of Reactant A at Extreme B
Go
Created
Rate Equation of Reactant A in G/L Reactions
Go
Created
Rate Equation of Reactant B at Extreme A
Go
Created
Rate Equation of Reactant B in G/L Reactions
Go
Created
Solid Loading
Go
Solid Catalyzed Reactions
(10)
Created
Effectiveness Factor at First Order
Go
Created
Initial Reactant Concentration for Rxn Containing Batch of Catalysts and Batch of Gas at 1st Order
Go
Created
Mass Transfer Coefficient of Fluid passing through Packed Bed of Particles
Go
Created
Mass Transfer Coefficient of Fluid passing through Single Particle
Go
Created
Rate Constant for Mixed Flow Reactor with Volume of Catalyst
Go
Created
Rate Constant for Mixed Flow Reactor with Weight of Catalyst
Go
Created
Rate of Reaction in Mixed Flow Reactor Containing Catalyst
Go
Created
Space Time of Mixed Flow Reactor with Volume of Catalyst
Go
Created
Space Time of Mixed Flow Reactor with Weight of Catalyst
Go
Created
Thiele Modulus
Go
Temperature and Pressure Effects
(9)
Created
Adiabatic Heat of Equilibrium Conversion
Go
Created
Equilibrium Conversion of Reaction at Final Temperature
Go
Created
Equilibrium Conversion of Reaction at Initial Temperature
Go
Created
Final Temperature for Equilibrium Conversion
Go
Created
Heat of Reaction at Equilibrium Conversion
Go
Created
Initial Temperature for Equilibrium Conversion
Go
Created
Non Adiabatic Heat of Equilibrium Conversion
Go
Created
Reactant Conversion at Adiabatic Conditions
Go
Created
Reactant Conversion at Non Adiabatic Conditions
Go
Various Fluidized Reactors
(10)
Created
Dimensionless Diameter for Fluidized Reactors at G/S Contacting Regime
Go
Created
Dimensionless Velocity for Fluidized Reactors at G/S Contacting Regime
Go
Created
Rate Constant of Phase between Bubble and Cloud
Go
Created
Rate Constant of Phase between Cloud-Wake and Emulsion
Go
Created
Rise Velocity of Bubble
Go
Created
Rise Velocity of Bubble in Bubbling Bed
Go
Created
Terminal Velocity of Fluid for Spherical Particles
Go
Created
Terminal Velocity of Fluids for Irregular Shaped Particles
Go
Created
Velocity in Fast Fluidized Bed
Go
Created
Velocity in Pneumatic Conveying
Go
Zero Order followed by First Order Reaction
(9)
Created
Initial Concentration of Reactant in Zero Order Reaction followed by First Order Reaction
Go
Created
Initial Reactant Concentration by Intermediate Conc. for Zero Order followed by First Order Rxn
Go
Created
Initial Reactant Concentration using Intermediate Conc. for Zero Order followed by First Order Rxn
Go
Created
Intermediate Concentration for Zero Order followed by First Order with Greater Rxn Time
Go
Created
Intermediate Concentration for Zero Order followed by First Order with Less Rxn Time
Go
Created
Maximum Intermediate Concentration in Zero Order followed by First Order
Go
Created
Rate Constant of Zero Order Reaction in Zero Order Reaction followed by First Order Reaction
Go
Created
Reactant Concentration of Zero Order Reaction followed by First Order Reaction
Go
Created
Time at Max Intermediate in Zero Order followed by First Order Reaction
Go
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