RMS University

Coming Soon!!

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RMS Fluid Catalytic Cracking (FCC) University

 

RMS Engineering, Inc. (RMS) is extremely excited to announce the upcoming schedule for the newly developed RMS FCC University. Below is a brief outline of the course, its benefits, as well as a selection of “menu” items that will be covered during this very unique learning opportunity.

Course Description

The development of this FCC-focused university is based on the ever-changing refining industry and its need for a better understanding of fluid catalytic cracking (FCC) and the many benefits of real-practical knowledge of FCC operations and valuable effects of optimized operations.

As mentioned, a “menu” of course subjects is attached to this announcement, from which your syllabus will be personally guided and taught by the industry’s leading FCC expert, Reza Sadeghbeigi.

Course Location

The University permanent location is,

5959 West Loop South, Suite 625

Bellaire, Texas  77401

Course Length

4-1/2 Days

Monday through Thursday

8 AM – 4 PM

Friday

8 AM – Noon

Class Size

3 (minimum) to 6 (maximum)

Fees

$2,500/participant

Who Should Attend: Process or operation engineers, design engineers and console operators.

 

MENU (Check “ü” Your Selection)

  1)    Fundamentals of Cat Cracking 3 Hrs     4) Unit Monitoring Tools 2.5 Hrs
·         Process overview

·         Chemistry of reactions

·         Feedstock properties

·         Basic process controls/instrumentation

·         Role of catalyst

·         Understanding heat balance

·         Mode of catalyst regeneration

·         Role of main fractionator & gas plant

·         Flue gas pollutants

·         Unit hazards

 

 

  ·      Fresh catalyst properties

·      E-cat properties

·      Diesel & residue content of the fresh feed

·      Total and basic nitrogen of the fresh feed

·      Hydrogen content of the fresh feed

·      Fresh catalyst, E-cat and additive usage

·      Slurry yield

·         Slurry oAPI gravity and ash content

·         Cat/Oil ratio

·         Hydrogen on coke

·         Regenerator superficial velocity and catalyst loading to cyclones

·         Cyclone velocities and pressure drops

·         Hydrogen/Methane ratio

·         C3/C4 recoveries

·         Review of APC set points

·         Catalyst Balance

Target audience:

·         Newly hired operators and engineers

·         Console operators

·         Unit and shift supervisor

  Target audience:

·         Process & Unit Engineers

 

  2)  Function of Major Equipment 3 Hrs     5) Sanity Checks of Operating Data and Heat Balance 1.5 Hrs
·         Standpipes

·         Slide and/or plug valves

·         Wye-piece or J-bend section

·         Feed nozzles

·         Riser

·         Cyclones /Trickle valves

·         Reactor stripper

·         Regenerator

·         Air and spent catalyst distributors

·         Flue gas slide valve and orifice chamber

·         Flue gas emission controls

  ·         Riser outlet temperature profile

·         Regenerator temperature profile

·         Raw versus actual catalyst bed levels

·         Pressure differentials across the slide /plug valves

·         Feed nozzles, stripping steam and other steam back pressures

·         Cyclone delta pressure

·         Catalyst flowing densities

·         Overall “heat of reaction”

·         Delta coke

·         Catalyst heat capacity

Target audience:

·         Unit operators

·         Mechanical engineers and Process engineers

·         Shift team managers

  Target audience:

·         Process engineers

·         Shift team supervisors

·         Console operators

 

  3)     Operating Conditions 2 Hrs     6) Sanity Checks of Reactor Yields 1.5 Hrs
·         Feed preheat temperature

·         Cracking temperature

·         Regenerator temperatures

·         Total air rate, carrier air, supplemental oxygen

·         Reactor & regenerator pressures

·         Catalyst circulation rate

·         Dispersion and stripping steam rates

·         HCO, slurry, naphtha recycle

·         Excess oxygen or CO2/CO ratio in the flue gas

  ·      Inert gas

·      H2S yield

·      Mass balance closure

·      Ratio of propylene to propane

·      Ratio of C4 olefins to total C4’s

·      Product distillation methods

·      Cut point adjusted yield

Target audience:

·         Console operators

·         Process engineers

·         Advance control engineers

·         Economic and planning engineers

  Target audience:

·         Process engineers

·         Economic and planning engineers

 

 

 

MENU

(Check “ü” Your Selection)

  7)      Catalyst Fluidization & Pressure Control 2.5 Hrs     10) Environmental Controls 2.0 Hrs
·         Standpipe fluidization

·         Impact of catalyst properties on fluidization

·         Reactor and regenerator catalyst levels

·         Pressure and density profiles in reactor-regenerator circuits

·         Importance of single-gauge pressure survey

  ·         CO

·         SOx

·         NOx

·         Particulates

·         Opacity

·         Gasoline Sulfur

·         Gasoline Benzene

Target audience:

·         Console operators

·         Unit engineers

·         Unit operators

  Target audience:

·         Environmental engineers

·         Console operators

·         Process engineers

 

  8) Main Fractionator and Gas Plant 2.5 Hrs     11) Equipment Design for Maximum
Reliability
3 Hrs
·         Role of the Main Fractionator & Gas Plant

·         Distillation principles

·         Heat integration

·         Product recovery and controls

·         Role of wet gas compressor

·         C3/C4 recovery

  ·         Standpipes

·         Slide and/or plug valves

·         Wye-piece or J-bend section

·         Feed nozzles

·         Riser

·         Reactor vapor line

·         Cyclones / Trickle valves

·         Reactor stripper

·         Regenerator

·         Air and spent catalyst distributors

·         Flue gas slide valve and orifice chamber

·         Expansion joints

Target audience:

·         Unit and console operators

·         Unit engineers

  Target audience:

·         Mechanical and maintenance engineers

·         Process engineers

 

  9)  Feed Diversion & Automatic Shutdown System 2 Hrs     12) Refractory Selection and Installation 3 Hrs
·         Cause & effect scenarios

·         Loss of air blower

·         Loss of feed rate

·         Loss of wet gas compressor

·         Low slide/plug valve pressure differential

·         High reactor catalyst bed level

·         Low riser outlet temperature

  ·         Purpose of refractory lining

·         Composition of refractory lining used in FCC

·         Properties

·         Choices of refractory lining & anchor systems

·         Refractory lining manufactures

·         Key quality control parameters to monitor

·         Installation techniques

·         Curing techniques

·         Failure mechanism

·         Specifications (general and job related)

Target audience:

·         Console and outside operators

·         Process and unit engineers

·         Reliability and advance control engineers

  Target audience:

·         Mechanical and reliability engineers

·         Process and unit engineers

 

 

MENU

(Check “ü” Your Selection)

  13) Troubleshooting 3 Hrs     16) Unit Optimization (No Capital) 2 Hrs
·         Excessive catalyst loss from reactor and/or regenerator

·         Excessive flue gas stack opacity

·         Erratic and inadequate catalyst circulation rate

·         Excessive afterburning

·         Excessive catalyst deactivation

·         Coking and fouling of slurry cooling circuit

·         Premature tower flooding and foaming

·         Expander fouling

·         Poor product yields

  ·         Understanding unit objectives and limitations

·         Feedstock quality & blend

·         Catalyst usage and formulation

·         Catalyst additives

·         Operating conditions

·         Pressure balance

·         Operating at reduced feed rates efficiently

Target audience:

·         Console and outside operators

·         Process and mechanical engineers

·         Shift team supervisors

  Target audience:

·         Process and unit engineers

·         Economic and planning engineers

·         Technical service managers

 

  14)    Unit Startup 3 Hrs     17) Unit Debottlenecking 2.5 Hrs
      (No Capital/Low Capital)
·         Key Punch List Items

·         Refractory drying/curing schedule

·         Main fractionator heat-up and dry out

·         Reactor – Fractionator isolation blind

·         Catalyst loading to prevent premature catalyst loss from regenerator

·         Purging and catalyst transfer to reactor system

·         Feed introduction – rate of feed injection rate

·         Unit “pressure bump” to clear obstruction

·         DCS display screens to display useful start up information

  ·         Combustion air limitation

·         Wet gas compressor limitation

·         Fresh feed hydraulics

·         Slide valve differential limitations

·         Catalyst circulation rate

·         Regenerator temperature

·         Regenerator superficial velocity

·         Tower flooding

·         Overhead cooling

·         Excessive dry gas yield

·         Environmental

Target audience:

·         Console and outside operators

·         Process and mechanical engineers

·         Shift team supervisors

  Target audience:

·         Process and unit engineers

·         Economic and planning engineers

·         Technical service managers

 

  15)  Available Technologies 2 Hrs     18) Capital Project Development and Turnaround Planning 1.5 Hrs
·         Feed & Catalyst Injection System

·         Riser Termination Device

·         Catalyst Stripping

·         Air & Spent Catalyst Distribution System

·         Catalyst Regeneration and Separation Systems

·         Flue Gas 3rd-stage Separators

·         Flue Gas Catalyst Emission Controls

·         Flue   Gas SO2/SO3 Controls

·         Flue Gas NOx Controls

·         Gasoline Sulfur Controls

·         Gasoline Benzene Controls

  ·         Front End Loading (FEL) evaluations

·         Obtaining meaningful total installed cost (TIC) estimates

·         Arriving at realist benefits

·         Lessons learned

Target audience:

·         Process and environmental engineers

·         Economic and planning engineers

·         Technical service and project managers

  Target audience:

·         Process and project engineers

·         Economic and planning engineers

 

 

 

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