REACTOR ENGINEERING
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Refining - Petrochemicals -
Chemicals - Engineering REACTOR ENGINEERING
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OBJECTIVES
▲ Who should
To give participants a general understanding of the main reactor engineering features and
attend? of the use of different types of multiphase flow reactors dedicated to refining industry.
Graduate engineers and On completion of the course, the participants:
engineering staff in charge – know the different kinds of reactor operations and their main associated parameters
of designing or operating – know the main features of gas liquid trickle bed reactor, gas-solid fluidized bed and
reactors in the oil refining gas-liquid-solid fluidized bed, including flow regimes and technologies, in relation to
field. processes such as hydrotreatment of distillates, hydroconversion of residue, FCC and
Fischer Tropsch.
COURSE CONTENT
Course pedagogy is based on real cases, discussed during the course.
REACTOR ENGINEERING: INTRODUCTION 0.5 day
The importance of multiphase flow, catalyst shape, contact and reaction parameters, e.g. contact
time, reaction kinetics, heat of reaction, deactivation.
Overview and analysis of these parameters through several examples of refining processes.
▲ Duration
REACTOR ENGINEERING: FUNDAMENTALS 1 day
5 days Ideal reactors: ideal concepts and theory of flow through reactors (CSTR and plug flow reactors,
CSTRs in series, axial dispersion, …). Concept and theory of residence time distribution in order
to characterize real systems.
External mass transfer limitations: mass transfer concept and theory through gas-liquid interphase
in reactive and non-reactive systems.
Internal mass transfer limitations: diffusion limitations of reactants through catalyst pores in
reactive systems (determination of internal mass transfer limitations).
▲ Dates & Location
GAS-LIQUID TRICKLE BED REACTORS (focus on HDT) 1.25 days
Non-scheduled Multiphase flow through fixed bed on trickle bed in relation to hydrotreatment HDT processes.
Main features and variables of HDT processes in refining industry.
May be organized for Flow regimes (trickle flow, pulsed flow, bubble flow); discussion on mapping as a function of
a single company operating conditions.
Relevant fixed bed properties (bed density and particle size) as well as their impact on operation.
Pressure drop throughout the bed as a function of operating conditions. Fluid and bed properties;
presentation of different models and correlations. Discussion.
Mass transfer limitation in the specific HDT case.
Design considerations. Understanding of the role of internals (tray distributors, quench systems).
Simple calculation methods enabling the estimation of reactor performances.
▲ Tuition Fees
To be agreed upon GAS-SOLID FLUIDIZED BED AND CIRCULATING FLUIDIZED
BEDS (focus on FCC) 1.5 days
FCC application: fluidized bed and circulating fluidized beds. Main features and variables of FCC
processes in the refining industry.
Fluidization regimes and mapping as a function of operating conditions. Bubble properties and
relevance on fluidized bed operation. Correlations are provided to estimate and describe fluidized
bed hydrodynamics.
Specific technologies related to fluidized bed and circulating fluidized beds:
▲ Course - standpipes enabling large catalyst circulation
Coordinator - gas distributors such as perforated plates, bubble caps, spargers and rings
- gas-solid separation systems such as negative or positive pressure cyclones
Philippe Bossennec Pressure balance of a circulating fluidized bed.
GAS-LIQUID SOLID FLUIDIZED BED
(focus on hydroconversion and Fischer-Tropsch) 0.75 day
Three phase fluidized bed: mainly hydroconversion and Fischer-Tropsch applications.
Ref. GCA / REACT-E Ebullated bed involving fludization of large particles: flow regimes, influence of operating conditions
and particle pproperties, description of bed hydrodynamics.
Slurry reactors involving fluidization of small particles: flow regimes, influence of operating
conditions and particles properties, description of bed hydrodynamics.
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