H5. Heat Transfer Handouts

Conduction through a Composite Layer

Conduction through a Cylindrical Body

Critical Radius of Insulation

Wall of Infinite Thickness Heated on One Side

Wall of Finite Thickness Heated on Both Sides

Finite Body Heated by a Fluid with Contact Resistance

Heat Loss from Extended Surfaces

Natural Convection - Air

Free Convection - Wet Steam

Fee Convection - Film Coefficient

Free Convection - Square Plate

Forced convection - Flow through Tube

Forced convection - Flow through annuli

Forced Convection - Clean Coefficient, Uc and Fouling Resist

Forced Convection - Flow through Tube

Forced Convection - Flow through annuli

Forced Convection - Shell and Tube Exchangers

Condensation in a Horizontal Tube

LMTD Correction Factors for Heat Exchangers

Optimum Arrangment of Fluids

Optimum Outlet Temperature - Shell and Tube Arrangement

Batch Process - Isothermal Heating of Batch Contents by

Batch Process - Non-Isothermal Batch Cooling

Batch Process - Heating of Tank Contents by an External Heat

Batch Process - Agitated vessel - Coil Immersed

Parallel Surfaces

Parallel Planes

Heat Loss due to Mixed Mode

Mixed Mode of Heat Transfer

Heat Loss due to Convection

Heat Loss from a buried pipe