Chemical Reactor Design and Catalyst Selection: Kinetics, Reactor Sizing and Deactivation – Paris, 12–16 Apr 2027
DestinationParis
Dates12 – 16 April 2027
Reference446_14142
This session
12–16 Apr 2027
This Chemical Reactor Design and Catalyst Selection: Kinetics, Reactor Sizing and Deactivation session in Paris runs from Monday 12 April to Friday 16 April 2027 (week 15, Q2 2027). It is the 2nd of 2 dates in Paris in 2027, at a fee of 23,500 SAR, the same for each of them. Registration is open for this date. It is held in person at Right Bank business hotel.
DatesMonday 12 Apr – Friday 16 Apr 2027
Week15 of 2027
Duration5 days
Fee23,500 SAR
StatusOpen for registration
FormatIn person
VenueRight Bank business hotel
Programme overview
Introduction:
Chemical reactor design decisions made on rough rate data, an unchecked reactor type or a catalyst chosen on price alone lead to lost selectivity, hot spots, short catalyst cycles and unplanned change-outs. This Core Concept course equips process and technical services engineers to derive rate laws from plant and pilot data, size and compare batch, CSTR and PFR reactors, control selectivity across multiple reactions, check heat removal against runaway, and select, monitor and regenerate catalysts in fixed, fluidised and trickle bed reactors. Participants build a Reactor Sizing and Catalyst Selection Workbook.
Course Objectives:
Derive rate laws and Arrhenius parameters from laboratory, pilot or plant data and express reactor results as conversion, yield and selectivity
Size batch, CSTR and PFR reactors from their design equations and justify the arrangement that meets a conversion target at least volume
Control selectivity in parallel and series reaction networks through temperature, concentration profile and reactor choice
Evaluate reactor energy balances and heat removal capacity to recognise the conditions that lead to hot spots and thermal runaway
Select a catalytic reactor type and catalyst on activity, selectivity, stability and pore diffusion limits, and plan protection against poisoning, sintering and coking
Monitor reactor and catalyst performance trends and diagnose common catalytic reactor problems in a Reactor Sizing and Catalyst Selection Workbook
Target Audience:
Process engineers responsible for reactor sizing, debottlenecking and operating targets in petrochemical and chemical plants
Technical services engineers who track catalyst activity, bed temperatures and run length on refinery and petrochemical reactors
Catalyst and licensing specialists who evaluate vendor proposals and catalyst change-out options
Process design engineers who prepare reactor datasheets for new units and revamps
Process safety engineers who review reactor heat removal and temperature excursion scenarios
Pilot plant and research engineers who generate kinetic data for scale-up
Course Outline:
Day 1: Reaction Kinetics, Rate Laws and Conversion Measures
Rate Law Forms: Power-Law, Reversible and Langmuir-Hinshelwood Expressions
Arrhenius Parameters: Activation Energy and Pre-Exponential Factor from Rate Data
Integral and Differential Methods for Fitting Pilot and Laboratory Kinetic Data
Conversion, Yield and Selectivity Definitions on a Reactor Stream Table
Equilibrium Conversion Limits from Gibbs Energy and Le Chatelier Shifts
Day 2: Ideal Reactor Models: Batch, CSTR and PFR Sizing
Batch and Semibatch Reactor Design Equation and Cycle Time Build-Up
CSTR Design Equation, Space Time and Levenspiel Plot Sizing
PFR Design Equation, Tubular Volume and Pressure Drop Along the Tube
CSTRs in Series Versus a Single PFR: Volume Comparison at Equal Conversion
Residence Time Distribution Tracer Tests and Non-Ideal Flow Diagnosis
Day 3: Multiple Reactions, Energy Balances and Heat Removal
Parallel and Series Reaction Networks: Instantaneous Versus Overall Selectivity
Selectivity Control by Temperature, Feed Distribution and Reactor Choice
Non-Isothermal Energy Balance and Adiabatic Temperature Rise Calculation
Thermal Runaway Awareness: Heat Generation Versus Removal Curves and Hot Spot Triggers
Day 4: Catalytic Reactors, Catalyst Selection and Deactivation
Fixed Bed, Fluidised Bed and Trickle Bed Reactor Selection Criteria
Catalyst Selection Matrix: Activity, Selectivity, Stability, Particle Shape and Size
Pore Diffusion Limits: Thiele Modulus and Effectiveness Factor
Deactivation Mechanisms: Poisoning, Sintering, Coking and Fouling Signatures
Regeneration by Coke Burn-Off and Guard Bed Protection Against Poisons
Day 5: Reactor Performance Monitoring, Troubleshooting and Workbook Build
Performance Monitoring: Weighted Average Bed Temperature, Pressure Drop and Activity Trends
Troubleshooting Cases: Channelling, Liquid Maldistribution, Hot Spots and Selectivity Loss
Modelling Exercise: Sizing a CSTR Train and a PFR for a Petrochemical Duty
Modelling Exercise: Catalyst Shortlist and Cycle Length Estimate for a Hydrogenation Service
Reactor Sizing and Catalyst Selection Workbook Assembly and Peer Review
Skills You Will Gain:
Kinetic Data Regression
Ideal Reactor Sizing
Residence Time Distribution Analysis
Selectivity Optimisation
Reactor Heat Balance Assessment
Catalyst Deactivation Diagnosis
Catalyst Vendor Evaluation
Catalytic Bed Performance Trending
Why Attend This Course:
Return with a Reactor Sizing and Catalyst Selection Workbook of checked calculations for a petrochemical or chemical duty
Challenge licensor and catalyst vendor claims on conversion, selectivity and cycle length with your own kinetic and diffusion estimates
Recognise early signs of hot spots, channelling and catalyst decline before they cost run length or safety margin
Exchange reactor and catalyst practice with engineers from refining, petrochemicals, fertilisers and specialty chemicals
Conclusion:
Reactor performance decides how much feed becomes saleable product and how long a catalyst charge lasts. The one week move from kinetics, rate laws and conversion measures through batch, CSTR and PFR sizing, multiple reactions, energy balances and heat removal, to fixed, fluidised and trickle bed reactors, catalyst selection, deactivation and regeneration. The final day applies these methods to monitoring and troubleshooting cases and closes with a Reactor Sizing and Catalyst Selection Workbook ready for technical review at work.
Chemical Reactor Design and Catalyst Selection: Kinetics, Reactor Sizing and Deactivation runs in Paris over 5 days, with 2 upcoming dates in Paris. The course fee is 23,500 SAR.
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