SlideShare una empresa de Scribd logo
1 de 13
•It would be impossible to determine what specific
problems are most usual to the Fluid Catalytic Cracking
Unit.
•There are more than 20 variations in mechanical designs
of the Regenerator and Reactor still operating throughout
the world and countless technology component designs
that have been applied either from licensor development
or refiner internal conception and fabrication .
•However, if a broad view is applied to the common
elements of all FCCU, then it is possible to define and
resolve the major problems that can be encountered
regardless of unit configuration.
FCC Troubleshooting
1
1. Poor Reactor Performance
• Poor reaction results occur when conversion and liquid
product yields do not match expected or predicted
results.
• This may be due to catalyst contamination and activity
but can also be related to other factors in the FCC Riser
such as feed and catalyst distribution.
• To achieve optimum yields, it is desirable to have
uniform catalyst density in the Riser.
• If the catalyst is poorly mixed with the feed, areas will
be formed in the Riser where there is either too much
feed and not enough catalyst and too much catalyst
and not enough feed.
2
1. Poor Reactor Performance
• If poor Riser hydrodynamics is suspected, the
following actions should be considered to
improve or alleviate the conditions.
• Vary Feed Dispersion Steam:
 feed dispersion steam provides the motive energy to generate
smaller oil droplets from the feed distributors
 outlet velocity to distribute the droplets into the catalyst and
decreases the hydrocarbon partial pressure at the feed
injection elevation to increase the oil-feed vaporization rate.
3
1. Poor Reactor Performance
• Survey and Review Riser Differential Pressure:
The Riser differential pressure is a relative
indicator of catalyst and oil mixing and
distribution.
Lower pressure drop signifies that there is less
catalyst back-mixing and a more uniform
density profile through the Riser.
4
1. Poor Reactor Performance
• Perform Riser Tracer Study:
radiation detection survey can be performed
This method can determine radial non-
uniformity of flow at various elevations in the
Riser.
Process conditions can be adjusted to minimize
or eliminate the mal-distribution and improve
conversion and yields.
5
2. Poor Regeneration
• The “ideal” Regenerator, at least in the dense
phase, with spent/stripped catalyst and air mixed
perfectly, with no mixing and separation zones,
and no boundary layers resulting in temperature
or concentration/density variations.
• The improper mixing can be radial or tangential
due to mis-design of, malfunction of, or damage
to systems used to introduce the catalyst and air
into the Regenerator and those for removing the
regenerated catalyst and flue gas out (Fig. 1)
6
2. Poor Regeneration
Fig 1.
Regenerator example showing possible hardware for introducing
air and spent catalyst. Note how the location of the standpipe
and pressure distribution in the air rings can affect mixing.
7
2. Poor Regeneration
• Another mode of improper mixing involves
the vertical jetting of air beyond the dense
bed surface into the dilute phase. (See Fig.2)
• This results in sub-optimal use of oxygen, not
to mention high catalyst losses into the flue
gas.
8
2. Poor Regeneration
Fig. 2
Jet penetration into dilute phase and vertical
mal-distribution of catalyst and air. 9
2. Poor Regeneration
• An additional key source of poor regeneration
is inadequate oxygen. This problem becomes
common as the FCC is pushed beyond original
design limits with higher feed rates and lower
quality (heavier) feeds.
10
2. Poor Regeneration
The following actions should be considered to improve
regenerator efficiency:
 Pressure surveys: Pressure surveys around the
Regenerator, particularly in the dense phase, can help
determine whether dead zones exist and whether
bypassing (jetting) is occurring.
 Temperature observations: These include tangential
and vertical wall or near-well temperatures and their
variation. Regions of unmixed (and un-regenerated) air
and spent catalyst are colder than well-mixed air and
catalyst.
11
2. Poor Regeneration
• Solutions for Inadequate Oxygen in Regenerator
depending on limitations on hardware and the
possibility of changing operations, the following
approaches are available:
Increasing air rate: This, more often than not,
requires either additional blowers or re-rating
existing blowers.
Oxygen enrichment: Using a richer source of oxygen
(instead of air) in order to deliver more oxygen using
the same blower, pressure, and temperature. Issues
of safety as well as cost are considerations.
Operational changes: Parameters, such Reactor
temperature, can be changed in order to decrease
coke formation. 12
FCC
Troubleshooting
1. Poor Reactor Performance
--Catalyst contamination
--Too much feed not enough catalyst and vice
versa
2. Poor Regeneration
-improper mixing of spent catalyst with air
- improper mixing involves the vertical jetting
of air beyond the dense bed surface into the
dilute phase
-inadequate oxygen in regenerator.
ACTIONS
1. Vary Feed
Dispersion Steam
2. Survey and Review
Riser Differential
Pressure
3. Perform Riser Tracer
Study
ACTIONS
1. Install possible hardware to introduce air and spent
catalyst.
2. Install the jet penetration into dilute phase and vertical
mal-distribution of catalyst and air
3. Pressure survey and Temperature observations to
improve generator efficiency
4. Increasing air rate, oxygen enrichment and operational
changes to solve inadequate oxygen in regenerator.
13

Más contenido relacionado

La actualidad más candente

PRESENTATION ON INPLANT TRAINING AT MRPL
PRESENTATION ON INPLANT TRAINING AT MRPLPRESENTATION ON INPLANT TRAINING AT MRPL
PRESENTATION ON INPLANT TRAINING AT MRPLAnkit Devatwal
 
Petroleum Refinery Engineering-Part-2-30-July-2016
Petroleum Refinery Engineering-Part-2-30-July-2016Petroleum Refinery Engineering-Part-2-30-July-2016
Petroleum Refinery Engineering-Part-2-30-July-2016Muhammad Rashid Usman
 
Chapter 2 crude_oil_processing2
Chapter 2 crude_oil_processing2Chapter 2 crude_oil_processing2
Chapter 2 crude_oil_processing2Helena Francis
 
5 oil refinery_processes
5 oil refinery_processes5 oil refinery_processes
5 oil refinery_processesGovind Manglani
 
Oil refinery industrial art
Oil refinery industrial artOil refinery industrial art
Oil refinery industrial artBRONSWERK
 
Refinery process-description
Refinery process-descriptionRefinery process-description
Refinery process-descriptionMing Deng Chai
 
Oil Refinery ----- An Intro
Oil Refinery ----- An IntroOil Refinery ----- An Intro
Oil Refinery ----- An IntroMuhammad Abbas
 
Hydrotreating process
Hydrotreating processHydrotreating process
Hydrotreating processtranslateds
 
Thermal cracking (2)
Thermal cracking (2)Thermal cracking (2)
Thermal cracking (2)Kumar
 
Chapter 6c -_ht_design_consideration_-_latest
Chapter 6c -_ht_design_consideration_-_latestChapter 6c -_ht_design_consideration_-_latest
Chapter 6c -_ht_design_consideration_-_latestHelena Francis
 
Visbreaking and Delayed coking
Visbreaking and Delayed cokingVisbreaking and Delayed coking
Visbreaking and Delayed cokingSanyam Jain
 
Chapter 6b -_hydrotreating_hds_catalyst
Chapter 6b -_hydrotreating_hds_catalystChapter 6b -_hydrotreating_hds_catalyst
Chapter 6b -_hydrotreating_hds_catalystHelena Francis
 

La actualidad más candente (20)

PRESENTATION ON INPLANT TRAINING AT MRPL
PRESENTATION ON INPLANT TRAINING AT MRPLPRESENTATION ON INPLANT TRAINING AT MRPL
PRESENTATION ON INPLANT TRAINING AT MRPL
 
Petroleum Refinery Engineering-Part-2-30-July-2016
Petroleum Refinery Engineering-Part-2-30-July-2016Petroleum Refinery Engineering-Part-2-30-July-2016
Petroleum Refinery Engineering-Part-2-30-July-2016
 
Refinery Basic
Refinery Basic Refinery Basic
Refinery Basic
 
Oil Refinery
Oil Refinery Oil Refinery
Oil Refinery
 
catalytic reforming
catalytic reformingcatalytic reforming
catalytic reforming
 
Chapter 2 crude_oil_processing2
Chapter 2 crude_oil_processing2Chapter 2 crude_oil_processing2
Chapter 2 crude_oil_processing2
 
5 oil refinery_processes
5 oil refinery_processes5 oil refinery_processes
5 oil refinery_processes
 
Oil refinery industrial art
Oil refinery industrial artOil refinery industrial art
Oil refinery industrial art
 
Petroleum refining (3 of 3)
Petroleum refining (3 of 3)Petroleum refining (3 of 3)
Petroleum refining (3 of 3)
 
Refinery process-description
Refinery process-descriptionRefinery process-description
Refinery process-description
 
Oil Refinery ----- An Intro
Oil Refinery ----- An IntroOil Refinery ----- An Intro
Oil Refinery ----- An Intro
 
Hydrotreating process
Hydrotreating processHydrotreating process
Hydrotreating process
 
Thermal cracking (2)
Thermal cracking (2)Thermal cracking (2)
Thermal cracking (2)
 
Chapter 6c -_ht_design_consideration_-_latest
Chapter 6c -_ht_design_consideration_-_latestChapter 6c -_ht_design_consideration_-_latest
Chapter 6c -_ht_design_consideration_-_latest
 
Internship_13BCH0001
Internship_13BCH0001Internship_13BCH0001
Internship_13BCH0001
 
Oil Refinery - Processes
Oil Refinery - ProcessesOil Refinery - Processes
Oil Refinery - Processes
 
Visbreaking and Delayed coking
Visbreaking and Delayed cokingVisbreaking and Delayed coking
Visbreaking and Delayed coking
 
Refinery basics
Refinery basicsRefinery basics
Refinery basics
 
2010 npra seminar, fundamentals of desalter operation
2010 npra seminar, fundamentals of desalter operation2010 npra seminar, fundamentals of desalter operation
2010 npra seminar, fundamentals of desalter operation
 
Chapter 6b -_hydrotreating_hds_catalyst
Chapter 6b -_hydrotreating_hds_catalystChapter 6b -_hydrotreating_hds_catalyst
Chapter 6b -_hydrotreating_hds_catalyst
 

Destacado

Chapter 6 -_comparison_ht_hc
Chapter 6 -_comparison_ht_hcChapter 6 -_comparison_ht_hc
Chapter 6 -_comparison_ht_hcHelena Francis
 
Chapter 5d hydrocracking
Chapter 5d hydrocrackingChapter 5d hydrocracking
Chapter 5d hydrocrackingHelena Francis
 
Chapter 6a -_hydrotreating
Chapter 6a -_hydrotreatingChapter 6a -_hydrotreating
Chapter 6a -_hydrotreatingHelena Francis
 
Каталог светодиодных светильников Geliomaster
Каталог светодиодных светильников GeliomasterКаталог светодиодных светильников Geliomaster
Каталог светодиодных светильников Geliomasterknkirnos
 
Vendéglátó iparban dolgozik? Panziója van? Sokszorozza meg velünk bevételét!
Vendéglátó iparban dolgozik? Panziója van? Sokszorozza meg velünk bevételét!Vendéglátó iparban dolgozik? Panziója van? Sokszorozza meg velünk bevételét!
Vendéglátó iparban dolgozik? Panziója van? Sokszorozza meg velünk bevételét!DXN ganoderma kávé
 
Silo Fire Fighting-Winning the Game of Hazards World Coal Dec16
Silo Fire Fighting-Winning the Game of Hazards World Coal Dec16Silo Fire Fighting-Winning the Game of Hazards World Coal Dec16
Silo Fire Fighting-Winning the Game of Hazards World Coal Dec16Justin Clift
 
Białka tatrzańska
Białka tatrzańskaBiałka tatrzańska
Białka tatrzańskatabmonika
 
Chapter 5f -sources_of_hydrogen_in_refinery_latest
Chapter 5f -sources_of_hydrogen_in_refinery_latestChapter 5f -sources_of_hydrogen_in_refinery_latest
Chapter 5f -sources_of_hydrogen_in_refinery_latestHelena Francis
 

Destacado (15)

Chapter 6 -_comparison_ht_hc
Chapter 6 -_comparison_ht_hcChapter 6 -_comparison_ht_hc
Chapter 6 -_comparison_ht_hc
 
Chapter 5d hydrocracking
Chapter 5d hydrocrackingChapter 5d hydrocracking
Chapter 5d hydrocracking
 
Chapter 6a -_hydrotreating
Chapter 6a -_hydrotreatingChapter 6a -_hydrotreating
Chapter 6a -_hydrotreating
 
Каталог светодиодных светильников Geliomaster
Каталог светодиодных светильников GeliomasterКаталог светодиодных светильников Geliomaster
Каталог светодиодных светильников Geliomaster
 
Vendéglátó iparban dolgozik? Panziója van? Sokszorozza meg velünk bevételét!
Vendéglátó iparban dolgozik? Panziója van? Sokszorozza meg velünk bevételét!Vendéglátó iparban dolgozik? Panziója van? Sokszorozza meg velünk bevételét!
Vendéglátó iparban dolgozik? Panziója van? Sokszorozza meg velünk bevételét!
 
Chapter 1
Chapter 1Chapter 1
Chapter 1
 
Chapter 4a heavy_oil2
Chapter 4a heavy_oil2Chapter 4a heavy_oil2
Chapter 4a heavy_oil2
 
Location recce
Location recceLocation recce
Location recce
 
Silo Fire Fighting-Winning the Game of Hazards World Coal Dec16
Silo Fire Fighting-Winning the Game of Hazards World Coal Dec16Silo Fire Fighting-Winning the Game of Hazards World Coal Dec16
Silo Fire Fighting-Winning the Game of Hazards World Coal Dec16
 
Cantón loja
Cantón lojaCantón loja
Cantón loja
 
SoftPay Mobile Deck
SoftPay Mobile DeckSoftPay Mobile Deck
SoftPay Mobile Deck
 
Białka tatrzańska
Białka tatrzańskaBiałka tatrzańska
Białka tatrzańska
 
Fractional distillation
Fractional distillationFractional distillation
Fractional distillation
 
Chapter 5f -sources_of_hydrogen_in_refinery_latest
Chapter 5f -sources_of_hydrogen_in_refinery_latestChapter 5f -sources_of_hydrogen_in_refinery_latest
Chapter 5f -sources_of_hydrogen_in_refinery_latest
 
Empresa deportiva
Empresa deportivaEmpresa deportiva
Empresa deportiva
 

Similar a Chapter 5e -_fcc_problems2

Solid Catalyzed Gas Phase Reactor Selection
Solid Catalyzed Gas Phase Reactor SelectionSolid Catalyzed Gas Phase Reactor Selection
Solid Catalyzed Gas Phase Reactor SelectionGerard B. Hawkins
 
Troubleshooting in FCC Unit
Troubleshooting in FCC UnitTroubleshooting in FCC Unit
Troubleshooting in FCC Unit?? ?
 
Avoid syn gas catalyst mal operation
Avoid syn gas catalyst mal operationAvoid syn gas catalyst mal operation
Avoid syn gas catalyst mal operationGerard B. Hawkins
 
68 optimize-troubleshoot-reactors
68 optimize-troubleshoot-reactors68 optimize-troubleshoot-reactors
68 optimize-troubleshoot-reactorsBaijan
 
PetroSkills: Best Tips of the Month
PetroSkills: Best Tips of the MonthPetroSkills: Best Tips of the Month
PetroSkills: Best Tips of the MonthWeston Shepherd
 
Maximizing Gas Turbine and Combined Cycle Capacity and Ratings
Maximizing Gas Turbine and Combined Cycle Capacity and RatingsMaximizing Gas Turbine and Combined Cycle Capacity and Ratings
Maximizing Gas Turbine and Combined Cycle Capacity and RatingsCary Campbell
 
Transformer & OLTC
Transformer & OLTCTransformer & OLTC
Transformer & OLTCRohit Dave
 
An insight into spray pulsed reactor through mathematical modeling of catalyt...
An insight into spray pulsed reactor through mathematical modeling of catalyt...An insight into spray pulsed reactor through mathematical modeling of catalyt...
An insight into spray pulsed reactor through mathematical modeling of catalyt...Siluvai Antony Praveen
 
The study and modeling of organic rankine cycle
The study and modeling of organic rankine cycleThe study and modeling of organic rankine cycle
The study and modeling of organic rankine cycleSulaiman Dawood Barry
 
METHANOL PLANT ARC RETROFIT Case Study
METHANOL PLANT ARC RETROFIT Case StudyMETHANOL PLANT ARC RETROFIT Case Study
METHANOL PLANT ARC RETROFIT Case StudyGerard B. Hawkins
 
Catalytic Reforming Technology - Infographics
Catalytic Reforming Technology - InfographicsCatalytic Reforming Technology - Infographics
Catalytic Reforming Technology - InfographicsGerard B. Hawkins
 
Field Experience from a Biotechnology Approach to Water Flood Improvement
Field Experience from a Biotechnology Approach to Water Flood ImprovementField Experience from a Biotechnology Approach to Water Flood Improvement
Field Experience from a Biotechnology Approach to Water Flood ImprovementBill-NewAERO
 
Syngas Catalyst Selection Criteria
Syngas Catalyst Selection CriteriaSyngas Catalyst Selection Criteria
Syngas Catalyst Selection CriteriaGerard B. Hawkins
 
Reciprocating Compressors.pdf
Reciprocating Compressors.pdfReciprocating Compressors.pdf
Reciprocating Compressors.pdfDWNLDUSRML
 
Chapter 3.1_Immiscible Gas Injection1.pdf
Chapter 3.1_Immiscible Gas Injection1.pdfChapter 3.1_Immiscible Gas Injection1.pdf
Chapter 3.1_Immiscible Gas Injection1.pdfTsaniSabila
 
Reactor kinetics & ; different types of reactor trays
Reactor kinetics & ; different types of reactor traysReactor kinetics & ; different types of reactor trays
Reactor kinetics & ; different types of reactor traysPrem Baboo
 
HVAC Preventive maintenance Presentation EVRaju
HVAC Preventive maintenance  Presentation EVRajuHVAC Preventive maintenance  Presentation EVRaju
HVAC Preventive maintenance Presentation EVRajuVenkata Raju Edarapalli
 
Enhancement of the Performance of Hydraulic Power Pack by Increasing Heat Dis...
Enhancement of the Performance of Hydraulic Power Pack by Increasing Heat Dis...Enhancement of the Performance of Hydraulic Power Pack by Increasing Heat Dis...
Enhancement of the Performance of Hydraulic Power Pack by Increasing Heat Dis...ijceronline
 
Reactor & Impeller Design in Hydrogenation
Reactor & Impeller Design in Hydrogenation Reactor & Impeller Design in Hydrogenation
Reactor & Impeller Design in Hydrogenation Gerard B. Hawkins
 

Similar a Chapter 5e -_fcc_problems2 (20)

Solid Catalyzed Gas Phase Reactor Selection
Solid Catalyzed Gas Phase Reactor SelectionSolid Catalyzed Gas Phase Reactor Selection
Solid Catalyzed Gas Phase Reactor Selection
 
Troubleshooting in FCC Unit
Troubleshooting in FCC UnitTroubleshooting in FCC Unit
Troubleshooting in FCC Unit
 
Avoid syn gas catalyst mal operation
Avoid syn gas catalyst mal operationAvoid syn gas catalyst mal operation
Avoid syn gas catalyst mal operation
 
68 optimize-troubleshoot-reactors
68 optimize-troubleshoot-reactors68 optimize-troubleshoot-reactors
68 optimize-troubleshoot-reactors
 
PetroSkills: Best Tips of the Month
PetroSkills: Best Tips of the MonthPetroSkills: Best Tips of the Month
PetroSkills: Best Tips of the Month
 
Maximizing Gas Turbine and Combined Cycle Capacity and Ratings
Maximizing Gas Turbine and Combined Cycle Capacity and RatingsMaximizing Gas Turbine and Combined Cycle Capacity and Ratings
Maximizing Gas Turbine and Combined Cycle Capacity and Ratings
 
Transformer & OLTC
Transformer & OLTCTransformer & OLTC
Transformer & OLTC
 
An insight into spray pulsed reactor through mathematical modeling of catalyt...
An insight into spray pulsed reactor through mathematical modeling of catalyt...An insight into spray pulsed reactor through mathematical modeling of catalyt...
An insight into spray pulsed reactor through mathematical modeling of catalyt...
 
HEP_Feb2013_EPA
HEP_Feb2013_EPAHEP_Feb2013_EPA
HEP_Feb2013_EPA
 
The study and modeling of organic rankine cycle
The study and modeling of organic rankine cycleThe study and modeling of organic rankine cycle
The study and modeling of organic rankine cycle
 
METHANOL PLANT ARC RETROFIT Case Study
METHANOL PLANT ARC RETROFIT Case StudyMETHANOL PLANT ARC RETROFIT Case Study
METHANOL PLANT ARC RETROFIT Case Study
 
Catalytic Reforming Technology - Infographics
Catalytic Reforming Technology - InfographicsCatalytic Reforming Technology - Infographics
Catalytic Reforming Technology - Infographics
 
Field Experience from a Biotechnology Approach to Water Flood Improvement
Field Experience from a Biotechnology Approach to Water Flood ImprovementField Experience from a Biotechnology Approach to Water Flood Improvement
Field Experience from a Biotechnology Approach to Water Flood Improvement
 
Syngas Catalyst Selection Criteria
Syngas Catalyst Selection CriteriaSyngas Catalyst Selection Criteria
Syngas Catalyst Selection Criteria
 
Reciprocating Compressors.pdf
Reciprocating Compressors.pdfReciprocating Compressors.pdf
Reciprocating Compressors.pdf
 
Chapter 3.1_Immiscible Gas Injection1.pdf
Chapter 3.1_Immiscible Gas Injection1.pdfChapter 3.1_Immiscible Gas Injection1.pdf
Chapter 3.1_Immiscible Gas Injection1.pdf
 
Reactor kinetics & ; different types of reactor trays
Reactor kinetics & ; different types of reactor traysReactor kinetics & ; different types of reactor trays
Reactor kinetics & ; different types of reactor trays
 
HVAC Preventive maintenance Presentation EVRaju
HVAC Preventive maintenance  Presentation EVRajuHVAC Preventive maintenance  Presentation EVRaju
HVAC Preventive maintenance Presentation EVRaju
 
Enhancement of the Performance of Hydraulic Power Pack by Increasing Heat Dis...
Enhancement of the Performance of Hydraulic Power Pack by Increasing Heat Dis...Enhancement of the Performance of Hydraulic Power Pack by Increasing Heat Dis...
Enhancement of the Performance of Hydraulic Power Pack by Increasing Heat Dis...
 
Reactor & Impeller Design in Hydrogenation
Reactor & Impeller Design in Hydrogenation Reactor & Impeller Design in Hydrogenation
Reactor & Impeller Design in Hydrogenation
 

Más de Helena Francis

Chapter 3 wax_processing_and_purification3
Chapter 3 wax_processing_and_purification3Chapter 3 wax_processing_and_purification3
Chapter 3 wax_processing_and_purification3Helena Francis
 
Chapter 11 ideal-distillation-systems (1)
Chapter 11 ideal-distillation-systems (1)Chapter 11 ideal-distillation-systems (1)
Chapter 11 ideal-distillation-systems (1)Helena Francis
 
Lecture 0 introduction(3)
Lecture 0 introduction(3)Lecture 0 introduction(3)
Lecture 0 introduction(3)Helena Francis
 
Chap 1 intro_to_engineering_calculations_1_student
Chap 1 intro_to_engineering_calculations_1_studentChap 1 intro_to_engineering_calculations_1_student
Chap 1 intro_to_engineering_calculations_1_studentHelena Francis
 

Más de Helena Francis (6)

Chapter 5a -_cracking
Chapter 5a -_crackingChapter 5a -_cracking
Chapter 5a -_cracking
 
Chapter 4 b4
Chapter 4 b4Chapter 4 b4
Chapter 4 b4
 
Chapter 3 wax_processing_and_purification3
Chapter 3 wax_processing_and_purification3Chapter 3 wax_processing_and_purification3
Chapter 3 wax_processing_and_purification3
 
Chapter 11 ideal-distillation-systems (1)
Chapter 11 ideal-distillation-systems (1)Chapter 11 ideal-distillation-systems (1)
Chapter 11 ideal-distillation-systems (1)
 
Lecture 0 introduction(3)
Lecture 0 introduction(3)Lecture 0 introduction(3)
Lecture 0 introduction(3)
 
Chap 1 intro_to_engineering_calculations_1_student
Chap 1 intro_to_engineering_calculations_1_studentChap 1 intro_to_engineering_calculations_1_student
Chap 1 intro_to_engineering_calculations_1_student
 

Último

University management System project report..pdf
University management System project report..pdfUniversity management System project report..pdf
University management System project report..pdfKamal Acharya
 
VIP Call Girls Ankleshwar 7001035870 Whatsapp Number, 24/07 Booking
VIP Call Girls Ankleshwar 7001035870 Whatsapp Number, 24/07 BookingVIP Call Girls Ankleshwar 7001035870 Whatsapp Number, 24/07 Booking
VIP Call Girls Ankleshwar 7001035870 Whatsapp Number, 24/07 Bookingdharasingh5698
 
Thermal Engineering Unit - I & II . ppt
Thermal Engineering  Unit - I & II . pptThermal Engineering  Unit - I & II . ppt
Thermal Engineering Unit - I & II . pptDineshKumar4165
 
VIP Call Girls Palanpur 7001035870 Whatsapp Number, 24/07 Booking
VIP Call Girls Palanpur 7001035870 Whatsapp Number, 24/07 BookingVIP Call Girls Palanpur 7001035870 Whatsapp Number, 24/07 Booking
VIP Call Girls Palanpur 7001035870 Whatsapp Number, 24/07 Bookingdharasingh5698
 
Top Rated Call Girls In chittoor 📱 {7001035870} VIP Escorts chittoor
Top Rated Call Girls In chittoor 📱 {7001035870} VIP Escorts chittoorTop Rated Call Girls In chittoor 📱 {7001035870} VIP Escorts chittoor
Top Rated Call Girls In chittoor 📱 {7001035870} VIP Escorts chittoordharasingh5698
 
Unleashing the Power of the SORA AI lastest leap
Unleashing the Power of the SORA AI lastest leapUnleashing the Power of the SORA AI lastest leap
Unleashing the Power of the SORA AI lastest leapRishantSharmaFr
 
Block diagram reduction techniques in control systems.ppt
Block diagram reduction techniques in control systems.pptBlock diagram reduction techniques in control systems.ppt
Block diagram reduction techniques in control systems.pptNANDHAKUMARA10
 
UNIT - IV - Air Compressors and its Performance
UNIT - IV - Air Compressors and its PerformanceUNIT - IV - Air Compressors and its Performance
UNIT - IV - Air Compressors and its Performancesivaprakash250
 
Thermal Engineering -unit - III & IV.ppt
Thermal Engineering -unit - III & IV.pptThermal Engineering -unit - III & IV.ppt
Thermal Engineering -unit - III & IV.pptDineshKumar4165
 
Hostel management system project report..pdf
Hostel management system project report..pdfHostel management system project report..pdf
Hostel management system project report..pdfKamal Acharya
 
Generative AI or GenAI technology based PPT
Generative AI or GenAI technology based PPTGenerative AI or GenAI technology based PPT
Generative AI or GenAI technology based PPTbhaskargani46
 
Minimum and Maximum Modes of microprocessor 8086
Minimum and Maximum Modes of microprocessor 8086Minimum and Maximum Modes of microprocessor 8086
Minimum and Maximum Modes of microprocessor 8086anil_gaur
 
Work-Permit-Receiver-in-Saudi-Aramco.pptx
Work-Permit-Receiver-in-Saudi-Aramco.pptxWork-Permit-Receiver-in-Saudi-Aramco.pptx
Work-Permit-Receiver-in-Saudi-Aramco.pptxJuliansyahHarahap1
 
VIP Model Call Girls Kothrud ( Pune ) Call ON 8005736733 Starting From 5K to ...
VIP Model Call Girls Kothrud ( Pune ) Call ON 8005736733 Starting From 5K to ...VIP Model Call Girls Kothrud ( Pune ) Call ON 8005736733 Starting From 5K to ...
VIP Model Call Girls Kothrud ( Pune ) Call ON 8005736733 Starting From 5K to ...SUHANI PANDEY
 
Bhosari ( Call Girls ) Pune 6297143586 Hot Model With Sexy Bhabi Ready For ...
Bhosari ( Call Girls ) Pune  6297143586  Hot Model With Sexy Bhabi Ready For ...Bhosari ( Call Girls ) Pune  6297143586  Hot Model With Sexy Bhabi Ready For ...
Bhosari ( Call Girls ) Pune 6297143586 Hot Model With Sexy Bhabi Ready For ...tanu pandey
 

Último (20)

Call Girls in Ramesh Nagar Delhi 💯 Call Us 🔝9953056974 🔝 Escort Service
Call Girls in Ramesh Nagar Delhi 💯 Call Us 🔝9953056974 🔝 Escort ServiceCall Girls in Ramesh Nagar Delhi 💯 Call Us 🔝9953056974 🔝 Escort Service
Call Girls in Ramesh Nagar Delhi 💯 Call Us 🔝9953056974 🔝 Escort Service
 
University management System project report..pdf
University management System project report..pdfUniversity management System project report..pdf
University management System project report..pdf
 
VIP Call Girls Ankleshwar 7001035870 Whatsapp Number, 24/07 Booking
VIP Call Girls Ankleshwar 7001035870 Whatsapp Number, 24/07 BookingVIP Call Girls Ankleshwar 7001035870 Whatsapp Number, 24/07 Booking
VIP Call Girls Ankleshwar 7001035870 Whatsapp Number, 24/07 Booking
 
Thermal Engineering Unit - I & II . ppt
Thermal Engineering  Unit - I & II . pptThermal Engineering  Unit - I & II . ppt
Thermal Engineering Unit - I & II . ppt
 
VIP Call Girls Palanpur 7001035870 Whatsapp Number, 24/07 Booking
VIP Call Girls Palanpur 7001035870 Whatsapp Number, 24/07 BookingVIP Call Girls Palanpur 7001035870 Whatsapp Number, 24/07 Booking
VIP Call Girls Palanpur 7001035870 Whatsapp Number, 24/07 Booking
 
Top Rated Call Girls In chittoor 📱 {7001035870} VIP Escorts chittoor
Top Rated Call Girls In chittoor 📱 {7001035870} VIP Escorts chittoorTop Rated Call Girls In chittoor 📱 {7001035870} VIP Escorts chittoor
Top Rated Call Girls In chittoor 📱 {7001035870} VIP Escorts chittoor
 
Call Girls in Netaji Nagar, Delhi 💯 Call Us 🔝9953056974 🔝 Escort Service
Call Girls in Netaji Nagar, Delhi 💯 Call Us 🔝9953056974 🔝 Escort ServiceCall Girls in Netaji Nagar, Delhi 💯 Call Us 🔝9953056974 🔝 Escort Service
Call Girls in Netaji Nagar, Delhi 💯 Call Us 🔝9953056974 🔝 Escort Service
 
Unleashing the Power of the SORA AI lastest leap
Unleashing the Power of the SORA AI lastest leapUnleashing the Power of the SORA AI lastest leap
Unleashing the Power of the SORA AI lastest leap
 
Block diagram reduction techniques in control systems.ppt
Block diagram reduction techniques in control systems.pptBlock diagram reduction techniques in control systems.ppt
Block diagram reduction techniques in control systems.ppt
 
UNIT - IV - Air Compressors and its Performance
UNIT - IV - Air Compressors and its PerformanceUNIT - IV - Air Compressors and its Performance
UNIT - IV - Air Compressors and its Performance
 
Thermal Engineering -unit - III & IV.ppt
Thermal Engineering -unit - III & IV.pptThermal Engineering -unit - III & IV.ppt
Thermal Engineering -unit - III & IV.ppt
 
Integrated Test Rig For HTFE-25 - Neometrix
Integrated Test Rig For HTFE-25 - NeometrixIntegrated Test Rig For HTFE-25 - Neometrix
Integrated Test Rig For HTFE-25 - Neometrix
 
Hostel management system project report..pdf
Hostel management system project report..pdfHostel management system project report..pdf
Hostel management system project report..pdf
 
Water Industry Process Automation & Control Monthly - April 2024
Water Industry Process Automation & Control Monthly - April 2024Water Industry Process Automation & Control Monthly - April 2024
Water Industry Process Automation & Control Monthly - April 2024
 
Generative AI or GenAI technology based PPT
Generative AI or GenAI technology based PPTGenerative AI or GenAI technology based PPT
Generative AI or GenAI technology based PPT
 
Minimum and Maximum Modes of microprocessor 8086
Minimum and Maximum Modes of microprocessor 8086Minimum and Maximum Modes of microprocessor 8086
Minimum and Maximum Modes of microprocessor 8086
 
Work-Permit-Receiver-in-Saudi-Aramco.pptx
Work-Permit-Receiver-in-Saudi-Aramco.pptxWork-Permit-Receiver-in-Saudi-Aramco.pptx
Work-Permit-Receiver-in-Saudi-Aramco.pptx
 
VIP Model Call Girls Kothrud ( Pune ) Call ON 8005736733 Starting From 5K to ...
VIP Model Call Girls Kothrud ( Pune ) Call ON 8005736733 Starting From 5K to ...VIP Model Call Girls Kothrud ( Pune ) Call ON 8005736733 Starting From 5K to ...
VIP Model Call Girls Kothrud ( Pune ) Call ON 8005736733 Starting From 5K to ...
 
Bhosari ( Call Girls ) Pune 6297143586 Hot Model With Sexy Bhabi Ready For ...
Bhosari ( Call Girls ) Pune  6297143586  Hot Model With Sexy Bhabi Ready For ...Bhosari ( Call Girls ) Pune  6297143586  Hot Model With Sexy Bhabi Ready For ...
Bhosari ( Call Girls ) Pune 6297143586 Hot Model With Sexy Bhabi Ready For ...
 
FEA Based Level 3 Assessment of Deformed Tanks with Fluid Induced Loads
FEA Based Level 3 Assessment of Deformed Tanks with Fluid Induced LoadsFEA Based Level 3 Assessment of Deformed Tanks with Fluid Induced Loads
FEA Based Level 3 Assessment of Deformed Tanks with Fluid Induced Loads
 

Chapter 5e -_fcc_problems2

  • 1. •It would be impossible to determine what specific problems are most usual to the Fluid Catalytic Cracking Unit. •There are more than 20 variations in mechanical designs of the Regenerator and Reactor still operating throughout the world and countless technology component designs that have been applied either from licensor development or refiner internal conception and fabrication . •However, if a broad view is applied to the common elements of all FCCU, then it is possible to define and resolve the major problems that can be encountered regardless of unit configuration. FCC Troubleshooting 1
  • 2. 1. Poor Reactor Performance • Poor reaction results occur when conversion and liquid product yields do not match expected or predicted results. • This may be due to catalyst contamination and activity but can also be related to other factors in the FCC Riser such as feed and catalyst distribution. • To achieve optimum yields, it is desirable to have uniform catalyst density in the Riser. • If the catalyst is poorly mixed with the feed, areas will be formed in the Riser where there is either too much feed and not enough catalyst and too much catalyst and not enough feed. 2
  • 3. 1. Poor Reactor Performance • If poor Riser hydrodynamics is suspected, the following actions should be considered to improve or alleviate the conditions. • Vary Feed Dispersion Steam:  feed dispersion steam provides the motive energy to generate smaller oil droplets from the feed distributors  outlet velocity to distribute the droplets into the catalyst and decreases the hydrocarbon partial pressure at the feed injection elevation to increase the oil-feed vaporization rate. 3
  • 4. 1. Poor Reactor Performance • Survey and Review Riser Differential Pressure: The Riser differential pressure is a relative indicator of catalyst and oil mixing and distribution. Lower pressure drop signifies that there is less catalyst back-mixing and a more uniform density profile through the Riser. 4
  • 5. 1. Poor Reactor Performance • Perform Riser Tracer Study: radiation detection survey can be performed This method can determine radial non- uniformity of flow at various elevations in the Riser. Process conditions can be adjusted to minimize or eliminate the mal-distribution and improve conversion and yields. 5
  • 6. 2. Poor Regeneration • The “ideal” Regenerator, at least in the dense phase, with spent/stripped catalyst and air mixed perfectly, with no mixing and separation zones, and no boundary layers resulting in temperature or concentration/density variations. • The improper mixing can be radial or tangential due to mis-design of, malfunction of, or damage to systems used to introduce the catalyst and air into the Regenerator and those for removing the regenerated catalyst and flue gas out (Fig. 1) 6
  • 7. 2. Poor Regeneration Fig 1. Regenerator example showing possible hardware for introducing air and spent catalyst. Note how the location of the standpipe and pressure distribution in the air rings can affect mixing. 7
  • 8. 2. Poor Regeneration • Another mode of improper mixing involves the vertical jetting of air beyond the dense bed surface into the dilute phase. (See Fig.2) • This results in sub-optimal use of oxygen, not to mention high catalyst losses into the flue gas. 8
  • 9. 2. Poor Regeneration Fig. 2 Jet penetration into dilute phase and vertical mal-distribution of catalyst and air. 9
  • 10. 2. Poor Regeneration • An additional key source of poor regeneration is inadequate oxygen. This problem becomes common as the FCC is pushed beyond original design limits with higher feed rates and lower quality (heavier) feeds. 10
  • 11. 2. Poor Regeneration The following actions should be considered to improve regenerator efficiency:  Pressure surveys: Pressure surveys around the Regenerator, particularly in the dense phase, can help determine whether dead zones exist and whether bypassing (jetting) is occurring.  Temperature observations: These include tangential and vertical wall or near-well temperatures and their variation. Regions of unmixed (and un-regenerated) air and spent catalyst are colder than well-mixed air and catalyst. 11
  • 12. 2. Poor Regeneration • Solutions for Inadequate Oxygen in Regenerator depending on limitations on hardware and the possibility of changing operations, the following approaches are available: Increasing air rate: This, more often than not, requires either additional blowers or re-rating existing blowers. Oxygen enrichment: Using a richer source of oxygen (instead of air) in order to deliver more oxygen using the same blower, pressure, and temperature. Issues of safety as well as cost are considerations. Operational changes: Parameters, such Reactor temperature, can be changed in order to decrease coke formation. 12
  • 13. FCC Troubleshooting 1. Poor Reactor Performance --Catalyst contamination --Too much feed not enough catalyst and vice versa 2. Poor Regeneration -improper mixing of spent catalyst with air - improper mixing involves the vertical jetting of air beyond the dense bed surface into the dilute phase -inadequate oxygen in regenerator. ACTIONS 1. Vary Feed Dispersion Steam 2. Survey and Review Riser Differential Pressure 3. Perform Riser Tracer Study ACTIONS 1. Install possible hardware to introduce air and spent catalyst. 2. Install the jet penetration into dilute phase and vertical mal-distribution of catalyst and air 3. Pressure survey and Temperature observations to improve generator efficiency 4. Increasing air rate, oxygen enrichment and operational changes to solve inadequate oxygen in regenerator. 13