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Calculators Created by Rishi Vadodaria

Rishi Vadodaria
Malviya National Institute Of Technology (MNIT JAIPUR ), JAIPUR
155
Formulas Created
3
Formulas Verified
8
Across Categories

List of Calculators by Rishi Vadodaria

Following is a combined list of all the calculators that have been created and verified by Rishi Vadodaria . Rishi Vadodaria has created 155 and verified 3 calculators across 8 different categories till date.
Adiabatic Saturation Temperature and Wet Bulb Temperature (1)
Verified Latent Heat of Air based on Adiabatic Saturation Temperature
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12 More Adiabatic Saturation Temperature and Wet Bulb Temperature Calculators
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Basic Formulas of Heat Exchanger Designs (45)
Created Allowable Length of Tube given Temperature Difference and Thermal Expansion of Tubes
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Created Baffle Spacing given Tube Length and Number of Baffles
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Created Channel Velocity of Fluid given Path Length and Plate Pressure Drop
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Created Equivalent Diameter for Square Pitch in Heat Exchanger
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Created Equivalent Diameter for Triangular Pitch in Heat Exchanger
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Created Heat Duty of Exchanger given Core Volume of Exchanger for Air Separation
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Created Heat Duty of Exchanger given Core Volume of Exchanger for Hydrocarbon Separation
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Created Heat Exchanger Volume for Air Separation Applications
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Created Heat Exchanger Volume for Hydrocarbon Applications
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Created Log Mean Temperature Difference in Plate Heat Exchanger Given Fluid Temperature and NTU
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Created Number of Baffles in Shell and Tube Heat Exchanger
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Created Number of Transfer Units for Plate Heat Exchanger
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Created Number of Tubes in Center Row Given Bundle Diameter and Tube Pitch
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Created Number of Tubes in Eight Pass Square Pitch given Bundle Diameter
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Created Number of Tubes in Eight Pass Triangular Pitch given Bundle Diameter
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Created Number of Tubes in Four Pass Square Pitch given Bundle Diameter
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Created Number of Tubes in Four Pass Triangular Pitch given Bundle Diameter
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Created Number of Tubes in One Pass Square Pitch given Bundle Diameter
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Created Number of Tubes in One Pass Triangular Pitch given Bundle Diameter
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Created Number of Tubes in Shell and Tube Heat Exchanger
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Created Number of Tubes in Six Pass Square Pitch given Bundle Diameter
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Created Number of Tubes in Six Pass Triangular Pitch given Bundle Diameter
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Created Number of Tubes in Two Pass Square Pitch given Bundle Diameter
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Created Number of Tubes in Two Pass Triangular Pitch given Bundle Diameter
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Created Outlet Temperature of Fluid in Plate Heat Exchanger given NTU and Log Mean Temperature Difference
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Created Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop
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Created Pressure Drop in Plate Type Heat Exchanger
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Created Pressure Drop of Vapor in Condensers given Vapors on Shell Side
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Created Provision for Thermal Expansion and Contraction in Heat Exchanger
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Created Pumping Power Required in Heat Exchanger Given Pressure Drop
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Created Reynolds Number for Condensate Film Inside Vertical Tubes in Condenser
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Created Reynolds Number for Condensate Film Outside Vertical Tubes in Heat Exchanger
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Created Shell Area for Heat Exchanger
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Created Shell Diameter of Heat Exchanger Given Clearance and Bundle Diameter
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Created Shell Side Pressure Drop in Heat Exchanger
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Created Stack Design Pressure Draft for Furnace
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Created Stack Height of Furnace given Design Pressure and Flue Gas Temperature
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Created Temperature Difference Achieved given Thermal Expansion and Length of Tubes in Heat Exchanger
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Created Tube Side Mass Flowrate Given Pumping Power and Tube Side Pressure Drop
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Created Tube Side Mass Flowrate of Liquid Given Number of Tubes and Fluid Velocity
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Created Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid
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Created Tube Side Pressure Drop in Heat Exchanger for Laminar Flow
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Created Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow
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Created Tube Side Velocity of Fluid Given Mass Flowrate and Number of Tubes
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Created Viscosity Correction Factor for Shell and Tube Heat Exchanger
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4 More Basic Formulas of Heat Exchanger Designs Calculators
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Bundle Diameter in Heat Exchanger (11)
Created Bundle Diameter for Eight Tube Pass Square Pitch in Heat Exchanger
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Created Bundle Diameter for Eight Tube Pass Triangular Pitch in Heat Exchanger
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Created Bundle Diameter for Four Tube Pass Square Pitch in Heat Exchanger
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Created Bundle Diameter for Four Tube Pass Triangular Pitch in Heat Exchanger
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Created Bundle Diameter for One Tube Pass Square Pitch in Heat Exchanger
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Created Bundle Diameter for One Tube Pass Triangular Pitch in Heat Exchanger
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Created Bundle Diameter for Six Tube Pass Square Pitch in Heat Exchanger
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Created Bundle Diameter for Six Tube Pass Triangular Pitch in Heat Exchanger
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Created Bundle Diameter for Two Tube Pass Square Pitch in Heat Exchanger
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Created Bundle Diameter for Two Tube Pass Triangular Pitch in Heat Exchanger
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Created Bundle Diameter given Number of Tubes in Centre Row and Pitch
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1 More Bundle Diameter in Heat Exchanger Calculators
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Crystallization (23)
Created Degree of Supersaturation given Solution Concentration and Equilibrium Saturation Value
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Created Equilibrium Saturation Value given Relative Supersaturation and Degree of Saturation
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Created Kinetic Driving Force in Crystallization given Chemical Potential of Fluid and Crystal
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Created Mass Flux Density given Mass Transfer Coefficient and Concentration Gradient
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Created Mass Flux Density given Reaction Rate Constant and Order of Integration Reaction
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Created Mass Transfer Coefficient given Mass Flux Density and Concentration Gradient
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Created Nucleation Rate for given Number of Particles and Volume of Constant Supersaturation
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Created Number of Particles given Nucleation Rate and Supersaturation Volume and Time
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Created Overall Excess Free Energy for Spherical Crystalline Body
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Created Reaction Rate Constant in Crystallization given Mass Flux Density and Order of Reaction
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Created Relative Supersaturation for given Supersaturation Ratio
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Created Relative Supersaturation given Degree of Saturation and Equilibrium Saturation Value
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Created Solubility Product given Activities of Species A and B
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Created Solubility Product given Activity Coefficient and Mole Fraction of Species A and B
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Created Solubility Product given Concentration of Species A and B
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Created Solution Concentration given Degree of Supersaturation and Equilibrium Saturation Value
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Created Supersaturation based on activities of Species A and B
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Created Supersaturation based on Concentration of Species A and B along with Solubility Product
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Created Supersaturation Ratio given Partial Pressure for Ideal Gas Condition
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Created Supersaturation Ratio given Solution Concentration and Equilibrium Saturation Value
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Created Supersaturation Time given Nucleation Rate and Supersaturation Volume
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Created Supersaturation Volume given Nucleation Rate and Supersaturation Time
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Created Suspension Density given Solid Density and Volumetric Holdup
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1 More Crystallization Calculators
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Deactivating Catalysts (2)
Verified Rate Constant based on Weight of Catalyst in Batch Solids and Batch Fluids
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Verified Rate Constant based on Weight of Catalyst in Batch Solids and Plug Constant Flow of Fluids
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13 More Deactivating Catalysts Calculators
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Distillation Tower Design (41)
Created Active Area given Gas Volumetric Flow and Flow Velocity
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Created Active Area Given Total Area and Fractional Downcomer Area
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Created Clearance Area under Downcomer given Weir Length and Apron Height
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Created Column Diameter Based on Vapor Flowrate and Mass Velocity of Vapor
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Created Column Diameter given Maximum Vapor Rate and Maximum Vapor Velocity
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Created Downcomer Liquid Load in Trays
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Created Downcomer Residence Time in Distillation Column
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Created Dry Plate Pressure Drop in Distillation Column Design
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Created External Reflux Ratio given Internal Reflux Ratio
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Created Flooding Velocity for given Flooding Constant
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Created Flooding Velocity in Distillation Column Design
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Created Fractional Active Area given Downcomer Area and Total Column Area
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Created Fractional Active Area given Fractional Downcomer Area
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Created Fractional Downcomer Area given Total Cross Sectional Area
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Created Head Loss in Downcomer of Tray Tower
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Created Height of Liquid Crest over Weir
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Created Internal Reflux Ratio Based on Liquid and Distillate Flowrates
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Created Internal Reflux Ratio Given External Reflux Ratio
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Created Length of Weir given Clearance Area and Apron Height of Tray
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Created Liquid Flowrate in Rectifying Section for given Quality of Feed
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Created Liquid Flowrate over Tray for given Dowcomer Liquid Load
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Created Liquid Vapor Flow Factor in Distillation Column Design
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Created Maximum Allowable Mass Velocity using Bubble Cap Trays
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Created Maximum Allowable Vapor Velocity given Plate Spacing and Fluid Densities
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Created Minimum External Reflux given Compositions
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Created Minimum Internal Reflux given Compositions
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Created Quality of Feed based on Enthalpy of Feed and Latent Heat of Vaporization
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Created Quality of Feed Based on Liquid Flowrates and Feed Flowrate
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Created Rectifying Section Flowrate of Liquid for given Quality of Feed
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Created Rectifying Section Flowrate of Vapor for given Quality of Feed
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Created Relative Volatility of Two Components Based on Normal Boiling Point and Latent Heat of Vaporization
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Created Residual Head Loss in Pressure in Distillation Column
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Created Souders and Brown Flooding Constant
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Created Stripping Section Flowrate of Liquid for given Quality of Feed
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Created Stripping Section Flowrate of Vapor for given Quality of Feed
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Created Tower Cross Sectional Area given Active Area
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Created Tower Cross Sectional Area given Fractional Active Area
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Created Tower Cross Sectional Area given Gas Volumetric Flow and Flooding Velocity
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Created Vapor Flowrate in Rectifying Section for given Quality of Feed
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Created Weep Fraction of Tray
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Created Weep Point Velocity in Distillation Column Design
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Heat Transfer Coefficient in Heat Exchangers (19)
Created Heat Transfer Coefficient for Condensation Inside Vertical Tubes
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Created Heat Transfer Coefficient for Condensation Outside Horizontal Tubes
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Created Heat Transfer Coefficient for Condensation Outside Vertical Tubes
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Created Heat Transfer Coefficient for Plate Heat Exchanger
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Created Heat Transfer Coefficient for Subcooling Inside Vertical Tubes
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Created Heat Transfer Coefficient for Subcooling Outside Horizontal Tubes
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Created Heat Transfer Coefficient for Water in Tube Side in Shell and Tube Heat Exchanger
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Created Heat Transfer Coefficient with Tube Loading for Condensation Inside Vertical Tubes
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Created Heat Transfer Coefficient with Tube Loading for Condensation Outside Horizontal Tubes
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Created Heat Transfer Coefficient with Tube Loading for Condensation Outside Vertical Tubes
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Created Horizontal Tube Loading for Outside Condensation
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Created Length of Tubes in Horizontal Condenser given Tube Loading and Condensate Flowrate
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Created Maximum Heat Flux in Evaporation Process
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Created Number of Tubes in Horizontal Condenser given Condensate Flowrate and Tube Loading
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Created Reynolds Number for Condensate Film given Tube Loading
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Created Shell Side Heat Transfer Coefficient
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Created Vertical Tube Loading for Inside Condensation
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Created Vertical Tube Loading for Outside Condensation
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Created Vertical Tube Loading given Reynolds Number for Condensate Film
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Packed Column Designing (16)
Created Average Specific Pressure Drop Given Top Bed Pressure Drop and Bottom Bed Pressure Drop
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Created Effective Interfacial Area of Packing using Onda's Method
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Created Gas Film Mass Transfer Coefficient given Column Performance and Interfacial Area
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Created Gas Flowrate given Column Performance and Interfacial Area
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Created Gas Molar Flux given Height of Transfer Unit and Interfacial Area
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Created Height of Overall Gas Phase Transfer Unit in Packed Column
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Created HETP of Packed Columns using 25 and 50mm Raschig Rings
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Created Interfacial Area given Height of Transfer Unit and Mass Transfer Coefficient
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Created Interfacial Area of Packing Given Performance of Column and Gas Flowrate
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Created Liquid Mass Film Coefficient in Packed Columns
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Created Log Mean Driving Force Based on Mole Fraction
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Created Number of Transfer Units for Dilute System in Packed Column
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Created Overall Gas Mass Transfer Coefficient given Height of Transfer Unit
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Created Performance of Column for Known Value of Height of Transfer Unit
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Created Performance of Column Given Gas-Film Transfer Coefficient and Vapor Flowrate
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Created Pressure Drop Correlation given Vapor Mass Flux and Packing Factor
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Percentage calculator Fraction calculator LCM HCF Calculator
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