Heat and Mass Transfer for Process Plants: Conduction, Convection, Radiation and Absorption – Paris, 1–12 Nov 2027
DestinationParis
Dates1 – 12 November 2027
Reference667_18584
This session
1–12 Nov 2027
This Heat and Mass Transfer for Process Plants: Conduction, Convection, Radiation and Absorption session in Paris runs from Monday 1 November to Friday 12 November 2027 (week 44, Q4 2027). It is the 2nd of 2 dates in Paris in 2027, at a fee of 42,300 SAR, the same for each of them. Registration is open for this date. It is held in person at Right Bank business hotel.
DatesMonday 1 Nov – Friday 12 Nov 2027
Week44 of 2027
Duration12 days
Fee42,300 SAR
StatusOpen for registration
FormatIn person
VenueRight Bank business hotel
Programme overview
Introduction:
Heat and mass transfer calculations sit behind almost every plant decision, yet many engineers rely on vendor figures or rules of thumb they cannot check, so insulation is under-specified, furnace tubes overheat, absorbers miss purity and cooling towers lose approach without explanation. This Core Concept course gives process, chemical and mechanical plant engineers a working method to calculate conduction, convection, boiling, condensation and radiation duties, quantify diffusion and mass transfer coefficients, and size absorption, drying and evaporative cooling steps. Participants assemble a Heat and Mass Transfer Calculation Pack for a case process unit.
Course Objectives:
Apply energy balances, steam properties and pressure drop methods to set the thermal and hydraulic basis for a plant heat or mass transfer calculation
Calculate conductive heat loss through walls, pipe insulation and finned surfaces and select an economic insulation thickness
Estimate convective, boiling, condensing and radiant heat transfer coefficients with suitable correlations for pipes, vessels, reboilers, condensers and fired heaters
Evaluate passive and active heat transfer enhancement options and transient heat-up or cool-down times against energy, friction and safety limits
Determine diffusion rates, mass transfer coefficients and transfer units for absorbers, strippers, dryers and humidifiers using heat-mass analogies
Build a calculation pack that links heat and mass transfer duties for a case process unit, including cooling tower and evaporator checks
Target Audience:
Process and chemical engineers who calculate unit duties, check operating margins and review thermal design data
Mechanical and static equipment engineers who specify insulation, heating jackets, tracing and fired equipment
Technical services engineers who investigate underperforming heaters, condensers, absorbers and dryers
Utility and energy engineers who run steam, cooling water and cooling tower systems
Plant design and project engineers who check vendor thermal and separation calculations
Course Outline:
Day 1: Applied Thermodynamics Refresher for Thermal Calculations
First Law Energy Balance on Open Systems with Shaft Work and Heat Duty
Enthalpy, Specific Heat and Latent Heat Data from Property Tables
Steam Tables and Mollier Chart for Saturated, Superheated and Flash Steam
Ideal Gas and Real Gas Behaviour with Compressibility Factor
Heat Duty Worksheet for Heating, Vaporising and Cooling Streams
Day 2: Fluid Flow Fundamentals Behind Heat and Mass Transfer
Reynolds Number Regimes and Velocity Profile Development in Pipes
Darcy Friction Factor from the Moody Chart and Colebrook Equation
Fitting Losses with K-Values and Equivalent Length Methods
Two-Phase Gas-Liquid Flow Patterns and Map Reading Overview
Boundary Layer Concept Linking Momentum and Thermal Layers
Day 3: Conduction Through Walls, Insulation and Extended Surfaces
Fourier Law and Thermal Conductivity of Metals, Refractories and Insulants
Composite Plane and Cylindrical Wall Resistance Networks
Critical Insulation Radius and Economic Insulation Thickness Calculation
Fin Efficiency and Extended Surface Effectiveness for Finned Tubes
Surface Temperature Check for Personnel Protection and Heat Tracing Loads
Day 4: Convection Correlations, Boiling and Condensation
Nusselt, Prandtl and Grashof Numbers in Forced and Natural Convection
Dittus-Boelter and Gnielinski Correlations for Turbulent Tube Flow
Natural Convection from Hot Vessels, Horizontal Pipes and Tank Walls
Pool and Flow Boiling Curve with Critical Heat Flux in Reboilers and Kettles
Film and Dropwise Condensation with Nusselt Theory for Condensers
Day 5: Radiation in Fired Equipment, Overall Coefficient and Week-One Case
Emissivity, View Factors and Grey Body Exchange in Furnace Radiant Sections
Flue Gas Radiation from Carbon Dioxide and Water Vapour Bands
Series Resistance Summation of Film, Wall and Deposit Terms
Fouling Allowance Effect on Required Area and Clean Versus Dirty Duty
Guided Case: Jacketed Reactor Heat-Up and Steam Main Heat Loss Calculation
Day 6: Heat Transfer Enhancement and Transient Heating and Cooling
Passive Enhancement with Twisted Tape, Coil-Spring and Rib Inserts
Rough Surfaces, Helically Coiled Tubes and Secondary Flow Effects
Enhancement Payback: Coefficient Gain Versus Friction and Pumping Penalty
Lumped Capacitance Method and Biot Number Test for Transient Heating
Heisler Chart Use for Slab, Cylinder and Sphere Cool-Down Times
Day 7: Mass Transfer Fundamentals: Diffusion, Coefficients and Analogies
Fick Law, Molecular Diffusivity and Equimolar Versus One-Way Diffusion
Film Theory, Penetration Theory and Two-Resistance Interface Model
Sherwood, Schmidt and Peclet Numbers in Mass Transfer Correlations
Chilton-Colburn J-Factor Analogy Linking Friction, Heat and Mass Transfer
Overall Gas-Phase and Liquid-Phase Mass Transfer Coefficient Estimation
Day 8: Gas Absorption and Stripping Calculations
Henry Law Equilibrium Data and Operating Line Construction
Minimum Solvent Rate and Absorption Factor Selection
Height of a Transfer Unit and Number of Transfer Units for Packed Columns
Stripping Factor and Steam or Air Stripper Performance Estimation
Packing Wetting, Flooding Approach and Their Effect on Transfer Rate
Day 9: Humidification, Drying and Simultaneous Heat and Mass Transfer
Psychrometric Chart Use: Humidity, Dew Point and Wet-Bulb Temperature
Drying Rate Curve with Constant-Rate and Falling-Rate Periods
Cooling Tower Range, Approach and Evaporation Loss Balance
Merkel Enthalpy Driving Force Method for Tower Characteristic
Single and Multiple-Effect Evaporator Steam Economy Overview
Day 10: Modelling Build: Heat and Mass Transfer Calculation Pack
Case Unit Data Sheet Review and Calculation Basis Agreement
Worked Calculation: Fired Heater Radiant Flux and Insulated Line Heat Loss
Worked Calculation: Absorber Transfer Units and Cooling Tower Approach Check
Sensitivity Runs on Fouling, Flow Rate and Ambient Wet-Bulb Temperature
Heat and Mass Transfer Calculation Pack Presentation and Peer Critique
Skills You Will Gain:
Thermal Duty Estimation
Insulation Thickness Selection
Convective Correlation Selection
Radiant Heat Flux Calculation
Transient Heat-Up Analysis
Transfer Unit Sizing
Psychrometric Analysis
Evaporative Cooling Assessment
Why Attend This Course:
Leave with a Heat and Mass Transfer Calculation Pack for a case process unit that can be adapted to equipment on your own site
Challenge vendor thermal and separation figures with hand calculations you can defend in design reviews
Explain lost heater, condenser, absorber or cooling tower performance to operations using transfer coefficients rather than guesswork
Work through calculations with process, chemical and mechanical engineers from refining, petrochemicals, power, fertiliser and water sectors
Conclusion:
Plant engineers who can calculate heat and mass transfer from first principles make sounder decisions on insulation, heaters, condensers, absorbers and cooling towers. Week one rebuilds thermodynamics, fluid flow, conduction, convection, phase change, radiation and the overall coefficient. Week two adds what a shorter course leaves out: enhancement economics, transient heating, diffusion and mass transfer coefficients, absorption and stripping, humidification, drying and evaporative cooling. The final day turns these methods into a Heat and Mass Transfer Calculation Pack for a case process unit.
Heat and Mass Transfer for Process Plants: Conduction, Convection, Radiation and Absorption runs in Paris over 12 days, with 2 upcoming dates in Paris. The course fee is 42,300 SAR.
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