Topic outline

  • General

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  • Mechanical Operations - Theory

    • Theory - Video Page
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    • Theory - Slides Page
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    • Quick Review of Mechanical Operations - Essential Formulas - Video Page
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    • Quick Review of Mechanical Operations - Essential Formulas - Slides Page
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  • Size Analysis

    • Sphericity of Cylinder Page
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    • Sphericity of Cube Page
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    • Sphericity of Various Shapes - Comparison Page
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      Mark as done
    • Sieve Analysis - Cumulative Oversize Page
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    • Sieve Analysis - Differential and Cumulative Plots Page
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    • Mesh Number for a Screen Opening Page
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    • Sieve Analysis - Fraction of Materials Retained between Two Meshes Page
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    • Volume Surface Mean Diameter Page
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    • Screen Effectiveness - Example-1 Page
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    • Screen Effectiveness - Example-2 Page
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  • Size Reduction

    • Energy Requirement for Crushing with Altered Particle Sizes Page
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    • Bonds Law for Estimating Energy for Size Reduction Page
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    • Power for Crushing from Bond's Law Page
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    • Time Required for Crushing Page
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    • Critical Speed of Ball Mill Page
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    • Diameter of Roll Crusher Page
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    • Roll Crusher - Maximum Diameter of Feed Page
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    • Theoretical Capacity of Roll Crusher Page
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  • Size Separation

    • Separation of Particles for Screening and Elutriation Page
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      Mark as done
    • Hydraulic Classifier Page
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    • Terminal Velocity vs Particle Diameter Page
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    • Settling Velocity vs. Density Page
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    • Hindered Settling Page
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    • Settling Velocity of Suspension to Terminal Velocity of Particle Page
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    • Separation Factor of Cyclone Page
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  • Filtration

    • Filtration - Equations Page
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    • Constant Rate and Constant Pressure Filtrations - Example-1 Page
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    • Constant Rate and Constant Pressure Filtrations - Example-2 Page
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    • Effect of Pressure Drop and Compressibility on Filtration Page
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    • Check for Incompressibility of Cake Page
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    • Time Required for Washing of Filtration Unit Page
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    • Constant Pressure Filtration - Conditions Page
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    • Constant Pressure Filtration Page
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    • Constant Pressure Filtration with Altered Area Page
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    • Pressure-drop vs Surface Area per Unit Volume of Particles Page
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    • Reduction of Filtration Time by Concentrating the Slurry Page
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    • Filter Medium Resistance Page
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    • Pressure-drop during Constant Rate Filtration Page
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    • Time for Washing of Filter Press Page
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  • Agitation

    • Power Required for Agitator Page
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    • Power vs Impeller Diameter at high Reynolds Number Page
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    • Agitator Scaleup - Power per Unit Volume Page
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    • Bio-Reactor Scaleup - Constant Tip-speed Page
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    • Power for the Scaled-up Mixer - Laminar Flow Page
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