Calculator A to Z

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
Go
12 More Adiabatic Saturation Temperature and Wet Bulb Temperature Calculators
Go
Basic Formulas Of Heat Exchanger Designs (46)
Created Allowable Length of Tube given Temperature Difference and Thermal Expansion of Tubes
Go
Created Baffle Spacing given Tube Length and Number of Baffles
Go
Created Bundle Diameter given Number of Tubes in Centre Row and Pitch
Go
Created Channel Velocity of Fluid given Path Length and Plate Pressure Drop
Go
Created Equivalent Diameter for Square Pitch in Heat Exchanger
Go
Created Equivalent Diameter for Triangular Pitch in Heat Exchanger
Go
Created Heat Duty of Exchanger given Core Volume of Exchanger for Air Separation
Go
Created Heat Duty of Exchanger given Core Volume of Exchanger for Hydrocarbon Separation
Go
Created Heat Exchanger Volume for Air Separation Applications
Go
Created Heat Exchanger Volume for Hydrocarbon Applications
Go
Created Log Mean Temperature Difference in Plate Heat Exchanger Given Fluid Temperature and NTU
Go
Created Number of Baffles in Shell and Tube Heat Exchanger
Go
Created Number of Transfer Units for Plate Heat Exchanger
Go
Created Number of Tubes in Center Row Given Bundle Diameter and Tube Pitch
Go
Created Number of Tubes in Eight Pass Square Pitch given Bundle Diameter
Go
Created Number of Tubes in Eight Pass Triangular Pitch given Bundle Diameter
Go
Created Number of Tubes in Four Pass Square Pitch given Bundle Diameter
Go
Created Number of Tubes in Four Pass Triangular Pitch given Bundle Diameter
Go
Created Number of Tubes in One Pass Square Pitch given Bundle Diameter
Go
Created Number of Tubes in One Pass Triangular Pitch given Bundle Diameter
Go
Created Number of Tubes in Shell and Tube Heat Exchanger
Go
Created Number of Tubes in Six Pass Square Pitch given Bundle Diameter
Go
Created Number of Tubes in Six Pass Triangular Pitch given Bundle Diameter
Go
Created Number of Tubes in Two Pass Square Pitch given Bundle Diameter
Go
Created Number of Tubes in Two Pass Triangular Pitch given Bundle Diameter
Go
Created Outlet Temperature of Fluid in Plate Heat Exchanger given NTU and Log Mean Temperature Difference
Go
Created Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop
Go
Created Pressure Drop in Plate Type Heat Exchanger
Go
Created Pressure Drop of Vapor in Condensers given Vapors on Shell Side
Go
Created Provision for Thermal Expansion and Contraction in Heat Exchanger
Go
Created Pumping Power Required in Heat Exchanger Given Pressure Drop
Go
Created Reynolds Number for Condensate Film Inside Vertical Tubes in Condenser
Go
Created Reynolds Number for Condensate Film Outside Vertical Tubes in Heat Exchanger
Go
Created Shell Area for Heat Exchanger
Go
Created Shell Diameter of Heat Exchanger Given Clearance and Bundle Diameter
Go
Created Shell Side Pressure Drop in Heat Exchanger
Go
Created Stack Design Pressure Draft for Furnace
Go
Created Stack Height of Furnace given Design Pressure and Flue Gas Temperature
Go
Created Temperature Difference Achieved given Thermal Expansion and Length of Tubes in Heat Exchanger
Go
Created Tube Side Mass Flowrate Given Pumping Power and Tube Side Pressure Drop
Go
Created Tube Side Mass Flowrate of Liquid Given Number of Tubes and Fluid Velocity
Go
Created Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid
Go
Created Tube Side Pressure Drop in Heat Exchanger for Laminar Flow
Go
Created Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow
Go
Created Tube Side Velocity of Fluid Given Mass Flowrate and Number of Tubes
Go
Created Viscosity Correction Factor for Shell and Tube Heat Exchanger
Go
5 More Basic Formulas Of Heat Exchanger Designs Calculators
Go
Bundle Diameter in Heat Exchanger (10)
Created Bundle Diameter for Eight Tube Pass Square Pitch in Heat Exchanger
Go
Created Bundle Diameter for Eight Tube Pass Triangular Pitch in Heat Exchanger
Go
Created Bundle Diameter for Four Tube Pass Square Pitch in Heat Exchanger
Go
Created Bundle Diameter for Four Tube Pass Triangular Pitch in Heat Exchanger
Go
Created Bundle Diameter for One Tube Pass Square Pitch in Heat Exchanger
Go
Created Bundle Diameter for One Tube Pass Triangular Pitch in Heat Exchanger
Go
Created Bundle Diameter for Six Tube Pass Square Pitch in Heat Exchanger
Go
Created Bundle Diameter for Six Tube Pass Triangular Pitch in Heat Exchanger
Go
Created Bundle Diameter for Two Tube Pass Square Pitch in Heat Exchanger
Go
Created Bundle Diameter for Two Tube Pass Triangular Pitch in Heat Exchanger
Go
Crystallization (23)
Created Degree of Supersaturation given Solution Concentration and Equilibrium Saturation Value
Go
Created Equilibrium Saturation Value given Relative Supersaturation and Degree of Saturation
Go
Created Kinetic Driving Force in Crystallization given Chemical Potential of Fluid and Crystal
Go
Created Mass Flux Density given Mass Transfer Coefficient and Concentration Gradient
Go
Created Mass Flux Density given Reaction Rate Constant and Order of Integration Reaction
Go
Created Mass Transfer Coefficient given Mass Flux Density and Concentration Gradient
Go
Created Nucleation Rate for given Number of Particles and Volume of Constant Supersaturation
Go
Created Number of Particles given Nucleation Rate and Supersaturation Volume and Time
Go
Created Overall Excess Free Energy for Spherical Crystalline Body
Go
Created Reaction Rate Constant in Crystallization given Mass Flux Density and Order of Reaction
Go
Created Relative Supersaturation for given Supersaturation Ratio
Go
Created Relative Supersaturation given Degree of Saturation and Equilibrium Saturation Value
Go
Created Solubility Product given Activities of Species A and B
Go
Created Solubility Product given Activity Coefficient and Mole Fraction of Species A and B
Go
Created Solubility Product given Concentration of Species A and B
Go
Created Solution Concentration given Degree of Supersaturation and Equilibrium Saturation Value
Go
Created Supersaturation based on activities of Species A and B
Go
Created Supersaturation based on Concentration of Species A and B along with Solubility Product
Go
Created Supersaturation Ratio given Partial Pressure for Ideal Gas Condition
Go
Created Supersaturation Ratio given Solution Concentration and Equilibrium Saturation Value
Go
Created Supersaturation Time given Nucleation Rate and Supersaturation Volume
Go
Created Supersaturation Volume given Nucleation Rate and Supersaturation Time
Go
Created Suspension Density given Solid Density and Volumetric Holdup
Go
1 More Crystallization Calculators
Go
Deactivating Catalysts (2)
Verified Rate Constant based on Weight of Catalyst in Batch Solids and Batch Fluids
Go
Verified Rate Constant based on Weight of Catalyst in Batch Solids and Plug Constant Flow of Fluids
Go
13 More Deactivating Catalysts Calculators
Go
Distillation Tower Design (41)
Created Active Area given Gas Volumetric Flow and Flow Velocity
Go
Created Active Area Given Total Area and Fractional Downcomer Area
Go
Created Clearance Area under Downcomer given Weir Length and Apron Height
Go
Created Column Diameter Based on Vapor Flowrate and Mass Velocity of Vapor
Go
Created Column Diameter given Maximum Vapor Rate and Maximum Vapor Velocity
Go
Created Downcomer Liquid Load in Trays
Go
Created Downcomer Residence Time in Distillation Column
Go
Created Dry Plate Pressure Drop in Distillation Column Design
Go
Created External Reflux Ratio given Internal Reflux Ratio
Go
Created Flooding Velocity for given Flooding Constant
Go
Created Flooding Velocity in Distillation Column Design
Go
Created Fractional Active Area given Downcomer Area and Total Column Area
Go
Created Fractional Active Area given Fractional Downcomer Area
Go
Created Fractional Downcomer Area given Total Cross Sectional Area
Go
Created Head Loss in Downcomer of Tray Tower
Go
Created Height of Liquid Crest over Weir
Go
Created Internal Reflux Ratio Based on Liquid and Distillate Flowrates
Go
Created Internal Reflux Ratio Given External Reflux Ratio
Go
Created Length of Weir given Clearance Area and Apron Height of Tray
Go
Created Liquid Flowrate in Rectifying Section for given Quality of Feed
Go
Created Liquid Flowrate over Tray for given Dowcomer Liquid Load
Go
Created Liquid Vapor Flow Factor in Distillation Column Design
Go
Created Maximum Allowable Mass Velocity using Bubble Cap Trays
Go
Created Maximum Allowable Vapor Velocity given Plate Spacing and Fluid Densities
Go
Created Minimum External Reflux given Compositions
Go
Created Minimum Internal Reflux given Compositions
Go
Created Quality of Feed based on Enthalpy of Feed and Latent Heat of Vaporization
Go
Created Quality of Feed Based on Liquid Flowrates and Feed Flowrate
Go
Created Rectifying Section Flowrate of Liquid for given Quality of Feed
Go
Created Rectifying Section Flowrate of Vapor for given Quality of Feed
Go
Created Relative Volatility of Two Components Based on Normal Boiling Point and Latent Heat of Vaporization
Go
Created Residual Head Loss in Pressure in Distillation Column
Go
Created Souders and Brown Flooding Constant
Go
Created Stripping Section Flowrate of Liquid for given Quality of Feed
Go
Created Stripping Section Flowrate of Vapor for given Quality of Feed
Go
Created Tower Cross Sectional Area given Active Area
Go
Created Tower Cross Sectional Area given Fractional Active Area
Go
Created Tower Cross Sectional Area given Gas Volumetric Flow and Flooding Velocity
Go
Created Vapor Flowrate in Rectifying Section for given Quality of Feed
Go
Created Weep Fraction of Tray
Go
Created Weep Point Velocity in Distillation Column Design
Go
Heat Transfer Coefficient in Heat Exchangers (19)
Created Heat Transfer Coefficient for Condensation Inside Vertical Tubes
Go
Created Heat Transfer Coefficient for Condensation Outside Horizontal Tubes
Go
Created Heat Transfer Coefficient for Condensation Outside Vertical Tubes
Go
Created Heat Transfer Coefficient for Plate Heat Exchanger
Go
Created Heat Transfer Coefficient for Subcooling Inside Vertical Tubes
Go
Created Heat Transfer Coefficient for Subcooling Outside Horizontal Tubes
Go
Created Heat Transfer Coefficient for Water in Tube Side in Shell and Tube Heat Exchanger
Go
Created Heat Transfer Coefficient with Tube Loading for Condensation Inside Vertical Tubes
Go
Created Heat Transfer Coefficient with Tube Loading for Condensation Outside Horizontal Tubes
Go
Created Heat Transfer Coefficient with Tube Loading for Condensation Outside Vertical Tubes
Go
Created Horizontal Tube Loading for Outside Condensation
Go
Created Length of Tubes in Horizontal Condenser given Tube Loading and Condensate Flowrate
Go
Created Maximum Heat Flux in Evaporation Process
Go
Created Number of Tubes in Horizontal Condenser given Condensate Flowrate and Tube Loading
Go
Created Reynolds Number for Condensate Film given Tube Loading
Go
Created Shell Side Heat Transfer Coefficient
Go
Created Vertical Tube Loading for Inside Condensation
Go
Created Vertical Tube Loading for Outside Condensation
Go
Created Vertical Tube Loading given Reynolds Number for Condensate Film
Go
Packed Column Designing (16)
Created Average Specific Pressure Drop Given Top Bed Pressure Drop and Bottom Bed Pressure Drop
Go
Created Effective Interfacial Area of Packing using Onda's Method
Go
Created Gas Film Mass Transfer Coefficient given Column Performance and Interfacial Area
Go
Created Gas Flowrate given Column Performance and Interfacial Area
Go
Created Gas Molar Flux given Height of Transfer Unit and Interfacial Area
Go
Created Height of Overall Gas Phase Transfer Unit in Packed Column
Go
Created HETP of Packed Columns using 25 and 50mm Raschig Rings
Go
Created Interfacial Area given Height of Transfer Unit and Mass Transfer Coefficient
Go
Created Interfacial Area of Packing Given Performance of Column and Gas Flowrate
Go
Created Liquid Mass Film Coefficient in Packed Columns
Go
Created Log Mean Driving Force Based on Mole Fraction
Go
Created Number of Transfer Units for Dilute System in Packed Column
Go
Created Overall Gas Mass Transfer Coefficient given Height of Transfer Unit
Go
Created Performance of Column for Known Value of Height of Transfer Unit
Go
Created Performance of Column Given Gas-Film Transfer Coefficient and Vapor Flowrate
Go
Created Pressure Drop Correlation given Vapor Mass Flux and Packing Factor
Go
About | Contact | Disclaimer | Terms | Privacy Policy
© 2016-2024 A softusvista inc. venture!


Home Icon
Home PDF Icon
FREE PDFs
🔍 Search
Category Icon
Categories
Share Icon
Share
Let Others Know
✖
Facebook
Twitter
Reddit
LinkedIn
Email
WhatsApp
Copied!