Selective Hydrogenation of the Steamcracker

HYDVAPO-EN-P

Who should attend?

  • To improve the knowledge of the selective hydrogenation processes of C2, C3, C4 cuts and pyrolysis gasolines (Pygas) for better controlling the operation.
Public :
  • Operating personnel of the steam cracker manufacturing units: experienced operators, panel operators, shift leaders and all technicians involved in the operation of these sections.

Level :Skilled

Prerequisite :
  • To fulfill at least one of the following criteria:
  • to have 1 year of proven professional experience in a steamcracker complex,
  • or to be in the process of moving to a position linked to operation in an steamcracker complex.

Course Content

  • SELECTIVE HYDROGENATION OF THE C2 CUT - Duration : 1.25 Days

      • Origin, characteristics and valuation of the C2 cut: origin and physical state of the cut, average composition, specifications of ethylene produced.
      • Identification of the impurity to be removed. Selection of the implementation of the treatment in relation to the nature of the impurity.
      • Location and operating principle of the selective hydrogenation section within the steamcracker: arrangement of the reactors, characteristics of the reactions involved in the process.
      • Nature, properties and mechanism of action of the catalyst: typical composition, activity, selectivity, main steps of the catalytic act, main well-known poisons (carbon monoxide, hydrogen sulfide, green oils...).
      • Analysis of the operating conditions: simplified process flow diagram (main process control loops, standard operating conditions, available analyzers) - Operating parameters (composition of the feedstock and hydrogen-rich gas, associated flow rates, CO content, molar ratio H2/acetylene, pressure, start-up temperature and Δt of the reactor...) - Performance monitoring (conversion rate, ethylene gain) - Analysis of some schematics of the DCS.
      • Case studies of adjustment: materialization of the evolution of the process using defined steps according to the variation of operating variables - Possible optimization points.
      • Possible major incidents, process safety and associated procedures.
  • SELECTIVE HYDROGENATION OF THE C3 CUT - Duration : 0.5 Day

      • Origin, characteristics and valuation of the cut C3: origin and physical state of the cut, average composition, specifications of the propylene produced.
      • Identification of the impurities to be removed. Selection of the implementation of the treatment in relation to the nature of the impurities.
      • Description of the main differences between the selective hydrogenation of the C2 section and that of the C3 section: location of the section, reactions involved, catalyst.
      • Simplified process flow diagram, operating conditions, driving parameters, performance monitoring, digital driving overviews and associated modules.
      • Case studies on the tuning of the unit: evolution of the process further to the modification of operating variables according to reference adjustments - Possible optimization points.
      • Possible major incidents, process safety and associated procedures.
  • SELECTIVE HYDROGENATION OF THE C4 CUT - Duration : 0.5 Day

      • Origin, characteristics and valuation of the cut C4: origin and physical state of the cut, average composition, specifications of the butadiene 1-3 produced.
      • Identification of the impurities to be removed, associated constraints - Simplified process flow diagram.
      • The main differences between the selective hydrogenation of the C4 cut and those of the C2 and C3 cuts.
      • Operating conditions and performances.
      • Process safety and associated procedures.
  • TREATMENT OF PYROLYSIS GASOLINES BY HYDROGENATION - Duration : 0.75 Day

      • Origin, characteristics and valuation of the C5+ cut (Pygas): origin and physical state of the cut, average composition.
      • Identification of the impurities to be eliminated, associated constraints - Simplified process flow diagram.
      • Selective hydrogenation 1st stage.
      • Types of catalysts according to the content and nature of the sulfur compounds of the feedstock.
      • Operating conditions and performance measurement.
      • Process safety and associated procedures.
      • Hydrogenation 2nd stage.
      • Role of section.
      • Types of catalysts.
      • Operating conditions and performance.

Learning Objectives

  • Attendees will be able to implement the following skills:
  • Identify key physico-chemical characteristics of the process,
  • Describe the process steps,
  • Justify process and operating safety measures.

Ways & Means

  • The content of this course can be adapted to the customer's needs. The pedagogy is focused on the units concerned, under cover of a secrecy agreement if necessary.
  • Case studies handled in groups, based on typical situations of conduct of the sections studied.
  • Possible contribution of experienced staff reporting his industrial experience of the operation on a daily basis.

Learning assessment

  • Quiz.

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Coordinator :IFP Training instructors, with expertise in the field and trained in modern teaching methods adapted to the specific needs of learners from the professional world.

To French entities : IFP Training is referenced to DataDock ; you may contact your OPCO about potential funding. Please contact our disabled persons referent to check the accessibility of this training program : referent.handicap@ifptraining.com