SlideShare a Scribd company logo
A R L
Process Optimization & Slop Oil
Reduction
2nd Plant Maintenance & Operations
Conference 2014
Muhammad Fahad Khan
Engineer Operations
• Challenge
• Slop Oil & its Sources
• Main Sources Detail
• Flash Point Calculator
• Achievements
• Q&A
Content of PresentationsA R L
“Approximately 8500 barrels per month of slop oil is
re-processed. Roughly reprocessing cost is 2$ / bbl. If
we reduce it to 5000 barrels per month, we can
reduce the cost by approximately 7000$ a month”
ChallengeA R L
SLOP OIL ???
Main Sources :
Process Units’ Sample Points
Desalter / JET Filters Drain
Process Units’ start up & Shut down
Upsets at Process Units
Vacuum Creating System
Slop Oil & its SourcesA R L
Process Unit Sample PointsA R L
CLOSE
SAMPLING
SYSTEM
REDUCE
SAMPLING
POINT DISTANCE
Process Unit Sample PointsA R L
CLOSE
SAMPLING
SYSTEM
REDUCE
SAMPLING
POINT DISTANCE
Distance b/w source
and sample point
Process Unit Sample Points
Blending with
HSD
550 bbls / month
A R L
(CONT’D)A R L
Slop Oil & SourcesCalculationsA R L
FLASH POINT CALCULATOR
FLASH OF COMPONENT “SLOP" 49 C
QUANTITY OF COMPONENT “SLOP" 550 BBLS
FLASH OF COMPONENT “Blended HSD" 72 C
QUANTITY OF COMPONENT "Blended HSD" 170 BBLS
FLASH OF COMPONENT BLEND 54 C
Slop Oil & Sources
Main Sources :
Units’ Sample Points
Desalter/ JET Filters Drain
Units’ start up Shut down
Upsets at units
Main Sources DetailA R L
TO HSD TANK
TO SLOP
JET Filters Drain
75 bbls /month
A R L
Slop Oil & SourcesCalculationsA R L
FLASH POINT CALCULATOR
FLASH OF COMPONENT “SLOP" 38 C
QUANTITY OF COMPONENT “SLOP" 75 BBLS
FLASH OF COMPONENT "Blended HSD" 72 C
QUANTITY OF COMPONENT "Blended HSD" 65 BBLS
FLASH OF COMPONENT BLEND 54 C
Slop Oil & Sources
Main Sources :
Units’ Sample Points
Desalter/ JET Filters Drain
Units’ start up Shut down
Upsets at units
Vacuum Creating System
Main Sources DetailA R L
Slop Oil & Sources
Main Sources :
Units’ Sample Points
Desalter/ JET Filters Drain
Units’ start up Shut down
Upsets at units
Vacuum Creating System
Main Sources DetailA R L
Slop Oil & Sources
Main Sources :
Units’ Sample Points
Desalter/ JET Filters Drain
Units’ start up Shut down
Upsets at units
Vacuum Creating System
Main Sources DetailA R L
OVER HEAD VESSEL
TO SLOP TANK
FOR RE-PROCESSING
Sampling Testing
Blending with HSD
Vacuum Creating System
Heavy Crude Unit (HCU)
1525 bbls / month
A R L
(Cont.)
A R L
Slop Oil & SourcesSlop Oil Results
Results of HCU Slop Oil From V-008
Sr. No
RESULTS
Sp.
Gravity
Color
(ASTM)
Flash Point
( C )
C.P
( C )
P. P
(C )
1 0.821 0.5 45 <-18 <-18
2 0.824 0.5 42 <-18 <-18
3 0.820 0.5 42 <-18 <-18
4 0.844 1.0 48 -9 -15
5 0.842 1.0 49 -9 -14
A R L
Slop Oil & SourcesCalculationsA R L
FLASH POINT CALCULATOR
FLASH OF COMPONENT “SLOP" 48 C
QUANTITY OF COMPONENT “SLOP" 1525 BBLS
FLASH OF COMPONENT "Blended HSD" 72 C
QUANTITY OF COMPONENT "Blended HSd" 550 BBLS
FLASH OF COMPONENT BLEND 54 C
HOT WELL
STORAGE TANK
LUMMUS SLOP REDUCTION
4210 bbls / month
A R L
LUMMUS SLOP REDUCTION
A R L
Slop Oil & SourcesSlop Oil Results
Results of Lummus Vacuum Separator / Tk-38
Sr. No
RESULTS
Sp. Gravity Color (ASTM) Flash Point ( C ) C.P ( C ) P. P (C )
1 0.838 0.5 56 <-18 <-18
2 0.842 0.5 55 -15 -18
3 0.835 0.5 58 <-18 <-18
4 0.825 0.5 60 <-18 <-18
5 0.831 0.5 46 <-18 <-18
6 0.837 1.0 47 <-18 <-18
7 0.833 1.0 51 <-18 <-18
8 0.829 0.5 51 <-18 <-18
9 0.845 0.5 57 2 -9
A R L
Slop Oil & SourcesCalculationsA R L
FLASH POINT CALCULATOR
FLASH OF COMPONENT “SLOP" 48 C
QUANTITY OF COMPONENT “SLOP" 4210 BBLS
FLASH OF COMPONENT "Blended HSD" 72 C
QUANTITY OF COMPONENT "Blended HSD" 1400 BBLS
FLASH OF COMPONENT BLEND 54 C
Slop Oil & Sources
Main Sources :
Units’ Sample Points
Desalter/ JET Filters Drain
Units’ start up Shut down
Upsets at units
Vacuum Creating System
Main Sources DetailA R L
Achievements
SLOP OIL RECOVERY DETAILS
DETAILS SLOP OIL
(TOTAL)
SLOP OIL
(Remaining)
SLOP OIL
(Recovered)
HSD
Required
(for
blending)
TOTAL
BLEND
Lummus (VCS)
4210 0 4210 1400 5610
HCU (VCS)
1525 0 1525 550 2075
Jp-1 Filter Repacking
75 0 75 65 140
SAMPLING Points &
Pump Drainages 3300 2750 550 170 720
TOTAL
9110 2750 6360 2185 8545
A R L
 6360 bbls of Slop Oil recovered.
 Reduction in SLOP OIL Re-Processing Cost
reduced for 6360 bbls/month.
 Blending of Recovered Oil with HSD,
meeting Quality Standards.
 One time profit of 6360 bbls excess HSD
Production with out processing.
A R L Achievements (cont.)
NO QUESTIONS ???
A R L
THANKS FOR ASKING

More Related Content

Viewers also liked

Modeling and Optimization of In-Situ Oil Production
Modeling and Optimization of In-Situ Oil ProductionModeling and Optimization of In-Situ Oil Production
Modeling and Optimization of In-Situ Oil Production
Alvaro Gil
 
Biogas technology - A renewable source of energy
Biogas technology - A renewable source of energyBiogas technology - A renewable source of energy
Biogas technology - A renewable source of energyJanak Shah
 
Crude-Oil Scheduling Technology: moving from simulation to optimization
Crude-Oil Scheduling Technology: moving from simulation to optimizationCrude-Oil Scheduling Technology: moving from simulation to optimization
Crude-Oil Scheduling Technology: moving from simulation to optimization
Brenno Menezes
 
INTEGRATED COW FARM-BIOGAS-ORGANIC FERTILIZER
INTEGRATED COW FARM-BIOGAS-ORGANIC FERTILIZERINTEGRATED COW FARM-BIOGAS-ORGANIC FERTILIZER
INTEGRATED COW FARM-BIOGAS-ORGANIC FERTILIZER
MARROS LESTARI
 
Biogas technology
Biogas technologyBiogas technology
Biogas technology
H Janardan Prabhu
 
Oil & gas
Oil & gasOil & gas
Oil & gas
Johhny Bravo
 
A Study Of Production Optimization Of An Oil Copy
A Study Of Production Optimization Of An Oil   CopyA Study Of Production Optimization Of An Oil   Copy
A Study Of Production Optimization Of An Oil Copy
aadrish
 
Biogas plant designs and engery calculations by ali saqlain
Biogas plant designs and engery calculations by ali saqlainBiogas plant designs and engery calculations by ali saqlain
Biogas plant designs and engery calculations by ali saqlain
ali saqlain
 
BIOGAS for Everyone : Simplified for all
BIOGAS for Everyone : Simplified for all BIOGAS for Everyone : Simplified for all
BIOGAS for Everyone : Simplified for all
Centre for Application of renewable Energy
 
Crude-Oil Blend Scheduling Optimization: An Application with Multi-Million D...
Crude-Oil Blend Scheduling Optimization:  An Application with Multi-Million D...Crude-Oil Blend Scheduling Optimization:  An Application with Multi-Million D...
Crude-Oil Blend Scheduling Optimization: An Application with Multi-Million D...
Alkis Vazacopoulos
 
Oil-Refinery Planning & Scheduling Optimization
Oil-Refinery Planning & Scheduling OptimizationOil-Refinery Planning & Scheduling Optimization
Oil-Refinery Planning & Scheduling OptimizationAlkis Vazacopoulos
 
Switching On The Biogas Resource - Renewable Energy from biogas
Switching On The Biogas Resource - Renewable Energy from biogasSwitching On The Biogas Resource - Renewable Energy from biogas
Switching On The Biogas Resource - Renewable Energy from biogas
SUEZ Australia & New Zealand
 

Viewers also liked (12)

Modeling and Optimization of In-Situ Oil Production
Modeling and Optimization of In-Situ Oil ProductionModeling and Optimization of In-Situ Oil Production
Modeling and Optimization of In-Situ Oil Production
 
Biogas technology - A renewable source of energy
Biogas technology - A renewable source of energyBiogas technology - A renewable source of energy
Biogas technology - A renewable source of energy
 
Crude-Oil Scheduling Technology: moving from simulation to optimization
Crude-Oil Scheduling Technology: moving from simulation to optimizationCrude-Oil Scheduling Technology: moving from simulation to optimization
Crude-Oil Scheduling Technology: moving from simulation to optimization
 
INTEGRATED COW FARM-BIOGAS-ORGANIC FERTILIZER
INTEGRATED COW FARM-BIOGAS-ORGANIC FERTILIZERINTEGRATED COW FARM-BIOGAS-ORGANIC FERTILIZER
INTEGRATED COW FARM-BIOGAS-ORGANIC FERTILIZER
 
Biogas technology
Biogas technologyBiogas technology
Biogas technology
 
Oil & gas
Oil & gasOil & gas
Oil & gas
 
A Study Of Production Optimization Of An Oil Copy
A Study Of Production Optimization Of An Oil   CopyA Study Of Production Optimization Of An Oil   Copy
A Study Of Production Optimization Of An Oil Copy
 
Biogas plant designs and engery calculations by ali saqlain
Biogas plant designs and engery calculations by ali saqlainBiogas plant designs and engery calculations by ali saqlain
Biogas plant designs and engery calculations by ali saqlain
 
BIOGAS for Everyone : Simplified for all
BIOGAS for Everyone : Simplified for all BIOGAS for Everyone : Simplified for all
BIOGAS for Everyone : Simplified for all
 
Crude-Oil Blend Scheduling Optimization: An Application with Multi-Million D...
Crude-Oil Blend Scheduling Optimization:  An Application with Multi-Million D...Crude-Oil Blend Scheduling Optimization:  An Application with Multi-Million D...
Crude-Oil Blend Scheduling Optimization: An Application with Multi-Million D...
 
Oil-Refinery Planning & Scheduling Optimization
Oil-Refinery Planning & Scheduling OptimizationOil-Refinery Planning & Scheduling Optimization
Oil-Refinery Planning & Scheduling Optimization
 
Switching On The Biogas Resource - Renewable Energy from biogas
Switching On The Biogas Resource - Renewable Energy from biogasSwitching On The Biogas Resource - Renewable Energy from biogas
Switching On The Biogas Resource - Renewable Energy from biogas
 

Similar to Process Optimization & Slop Oil Reduction( Fahad Khan)

Orifice Restrictors - Design Guidelines
Orifice Restrictors - Design GuidelinesOrifice Restrictors - Design Guidelines
Orifice Restrictors - Design Guidelines
Gerard B. Hawkins
 
Reactor and Catalyst Design
Reactor and Catalyst DesignReactor and Catalyst Design
Reactor and Catalyst Design
Gerard B. Hawkins
 
CRUDE ASSAY Non-Tech Oct 2015 BC
CRUDE ASSAY Non-Tech Oct 2015 BCCRUDE ASSAY Non-Tech Oct 2015 BC
CRUDE ASSAY Non-Tech Oct 2015 BCBruce Carlile
 
Husqvarna 165 r clearing saw service repair manual
Husqvarna 165 r clearing saw service repair manualHusqvarna 165 r clearing saw service repair manual
Husqvarna 165 r clearing saw service repair manual
fjskemdzaqmme
 
Distillation Sequences, Complex Columns and Heat Integration
Distillation Sequences, Complex Columns and Heat IntegrationDistillation Sequences, Complex Columns and Heat Integration
Distillation Sequences, Complex Columns and Heat Integration
Gerard B. Hawkins
 
Husqvarna 165 r clearing saw service repair manual
Husqvarna 165 r clearing saw service repair manualHusqvarna 165 r clearing saw service repair manual
Husqvarna 165 r clearing saw service repair manual
fjjskekkdmme
 
BIO2.1 Understanding Diesel Fuel
BIO2.1 Understanding Diesel FuelBIO2.1 Understanding Diesel Fuel
BIO2.1 Understanding Diesel Fuel
Biodiesel Automotive
 
EXPERIMENTAL INVESTIGATION ON PERFORMANCE AND EMISSION ANALYSIS OF SINGLE CYL...
EXPERIMENTAL INVESTIGATION ON PERFORMANCE AND EMISSION ANALYSIS OF SINGLE CYL...EXPERIMENTAL INVESTIGATION ON PERFORMANCE AND EMISSION ANALYSIS OF SINGLE CYL...
EXPERIMENTAL INVESTIGATION ON PERFORMANCE AND EMISSION ANALYSIS OF SINGLE CYL...
IRJET Journal
 
Shaft Couplings for Special Purpose Rotary Machines
Shaft Couplings for Special Purpose Rotary MachinesShaft Couplings for Special Purpose Rotary Machines
Shaft Couplings for Special Purpose Rotary Machines
Gerard B. Hawkins
 
Selection of Reboilers for Distillation Columns
Selection of Reboilers for Distillation ColumnsSelection of Reboilers for Distillation Columns
Selection of Reboilers for Distillation Columns
Gerard B. Hawkins
 
Reactor & Impeller Design in Hydrogenation
Reactor & Impeller Design in Hydrogenation Reactor & Impeller Design in Hydrogenation
Reactor & Impeller Design in Hydrogenation
Gerard B. Hawkins
 
Integration of Rotary Positive Displacement Pumps into a Process
Integration of Rotary Positive Displacement Pumps into a ProcessIntegration of Rotary Positive Displacement Pumps into a Process
Integration of Rotary Positive Displacement Pumps into a Process
Gerard B. Hawkins
 
1 palmer international consulting_presentation_artc_singapore_2014 (10)
1 palmer international consulting_presentation_artc_singapore_2014 (10)1 palmer international consulting_presentation_artc_singapore_2014 (10)
1 palmer international consulting_presentation_artc_singapore_2014 (10)
pipllp
 
Design and Rating of Trayed Distillation Columns
Design and Rating  of Trayed Distillation ColumnsDesign and Rating  of Trayed Distillation Columns
Design and Rating of Trayed Distillation Columns
Gerard B. Hawkins
 
BIO3.0 Biodiesel Performance and Vehicle Maintenance
BIO3.0 Biodiesel Performance and Vehicle MaintenanceBIO3.0 Biodiesel Performance and Vehicle Maintenance
BIO3.0 Biodiesel Performance and Vehicle Maintenance
Biodiesel Automotive
 
Estimation of Pressure Drop in Pipe Systems
Estimation of Pressure Drop in Pipe SystemsEstimation of Pressure Drop in Pipe Systems
Estimation of Pressure Drop in Pipe Systems
Gerard B. Hawkins
 
Calculation of an Ammonia Plant Energy Consumption:
Calculation of an Ammonia Plant Energy Consumption:  Calculation of an Ammonia Plant Energy Consumption:
Calculation of an Ammonia Plant Energy Consumption:
Gerard B. Hawkins
 
Gas Mixing
Gas MixingGas Mixing
Gas Mixing
Gerard B. Hawkins
 

Similar to Process Optimization & Slop Oil Reduction( Fahad Khan) (20)

Orifice Restrictors - Design Guidelines
Orifice Restrictors - Design GuidelinesOrifice Restrictors - Design Guidelines
Orifice Restrictors - Design Guidelines
 
Reactor and Catalyst Design
Reactor and Catalyst DesignReactor and Catalyst Design
Reactor and Catalyst Design
 
CRUDE ASSAY Non-Tech Oct 2015 BC
CRUDE ASSAY Non-Tech Oct 2015 BCCRUDE ASSAY Non-Tech Oct 2015 BC
CRUDE ASSAY Non-Tech Oct 2015 BC
 
Husqvarna 165 r clearing saw service repair manual
Husqvarna 165 r clearing saw service repair manualHusqvarna 165 r clearing saw service repair manual
Husqvarna 165 r clearing saw service repair manual
 
Distillation Sequences, Complex Columns and Heat Integration
Distillation Sequences, Complex Columns and Heat IntegrationDistillation Sequences, Complex Columns and Heat Integration
Distillation Sequences, Complex Columns and Heat Integration
 
Husqvarna 165 r clearing saw service repair manual
Husqvarna 165 r clearing saw service repair manualHusqvarna 165 r clearing saw service repair manual
Husqvarna 165 r clearing saw service repair manual
 
BIO2.1 Understanding Diesel Fuel
BIO2.1 Understanding Diesel FuelBIO2.1 Understanding Diesel Fuel
BIO2.1 Understanding Diesel Fuel
 
EXPERIMENTAL INVESTIGATION ON PERFORMANCE AND EMISSION ANALYSIS OF SINGLE CYL...
EXPERIMENTAL INVESTIGATION ON PERFORMANCE AND EMISSION ANALYSIS OF SINGLE CYL...EXPERIMENTAL INVESTIGATION ON PERFORMANCE AND EMISSION ANALYSIS OF SINGLE CYL...
EXPERIMENTAL INVESTIGATION ON PERFORMANCE AND EMISSION ANALYSIS OF SINGLE CYL...
 
Shaft Couplings for Special Purpose Rotary Machines
Shaft Couplings for Special Purpose Rotary MachinesShaft Couplings for Special Purpose Rotary Machines
Shaft Couplings for Special Purpose Rotary Machines
 
Selection of Reboilers for Distillation Columns
Selection of Reboilers for Distillation ColumnsSelection of Reboilers for Distillation Columns
Selection of Reboilers for Distillation Columns
 
Understanding Diesel Fuel
Understanding Diesel FuelUnderstanding Diesel Fuel
Understanding Diesel Fuel
 
PPT final
PPT finalPPT final
PPT final
 
Reactor & Impeller Design in Hydrogenation
Reactor & Impeller Design in Hydrogenation Reactor & Impeller Design in Hydrogenation
Reactor & Impeller Design in Hydrogenation
 
Integration of Rotary Positive Displacement Pumps into a Process
Integration of Rotary Positive Displacement Pumps into a ProcessIntegration of Rotary Positive Displacement Pumps into a Process
Integration of Rotary Positive Displacement Pumps into a Process
 
1 palmer international consulting_presentation_artc_singapore_2014 (10)
1 palmer international consulting_presentation_artc_singapore_2014 (10)1 palmer international consulting_presentation_artc_singapore_2014 (10)
1 palmer international consulting_presentation_artc_singapore_2014 (10)
 
Design and Rating of Trayed Distillation Columns
Design and Rating  of Trayed Distillation ColumnsDesign and Rating  of Trayed Distillation Columns
Design and Rating of Trayed Distillation Columns
 
BIO3.0 Biodiesel Performance and Vehicle Maintenance
BIO3.0 Biodiesel Performance and Vehicle MaintenanceBIO3.0 Biodiesel Performance and Vehicle Maintenance
BIO3.0 Biodiesel Performance and Vehicle Maintenance
 
Estimation of Pressure Drop in Pipe Systems
Estimation of Pressure Drop in Pipe SystemsEstimation of Pressure Drop in Pipe Systems
Estimation of Pressure Drop in Pipe Systems
 
Calculation of an Ammonia Plant Energy Consumption:
Calculation of an Ammonia Plant Energy Consumption:  Calculation of an Ammonia Plant Energy Consumption:
Calculation of an Ammonia Plant Energy Consumption:
 
Gas Mixing
Gas MixingGas Mixing
Gas Mixing
 

Process Optimization & Slop Oil Reduction( Fahad Khan)

  • 1. A R L Process Optimization & Slop Oil Reduction 2nd Plant Maintenance & Operations Conference 2014 Muhammad Fahad Khan Engineer Operations
  • 2. • Challenge • Slop Oil & its Sources • Main Sources Detail • Flash Point Calculator • Achievements • Q&A Content of PresentationsA R L
  • 3. “Approximately 8500 barrels per month of slop oil is re-processed. Roughly reprocessing cost is 2$ / bbl. If we reduce it to 5000 barrels per month, we can reduce the cost by approximately 7000$ a month” ChallengeA R L
  • 4. SLOP OIL ??? Main Sources : Process Units’ Sample Points Desalter / JET Filters Drain Process Units’ start up & Shut down Upsets at Process Units Vacuum Creating System Slop Oil & its SourcesA R L
  • 5. Process Unit Sample PointsA R L CLOSE SAMPLING SYSTEM REDUCE SAMPLING POINT DISTANCE
  • 6. Process Unit Sample PointsA R L CLOSE SAMPLING SYSTEM REDUCE SAMPLING POINT DISTANCE Distance b/w source and sample point
  • 7. Process Unit Sample Points Blending with HSD 550 bbls / month A R L
  • 9. Slop Oil & SourcesCalculationsA R L FLASH POINT CALCULATOR FLASH OF COMPONENT “SLOP" 49 C QUANTITY OF COMPONENT “SLOP" 550 BBLS FLASH OF COMPONENT “Blended HSD" 72 C QUANTITY OF COMPONENT "Blended HSD" 170 BBLS FLASH OF COMPONENT BLEND 54 C
  • 10. Slop Oil & Sources Main Sources : Units’ Sample Points Desalter/ JET Filters Drain Units’ start up Shut down Upsets at units Main Sources DetailA R L
  • 11. TO HSD TANK TO SLOP JET Filters Drain 75 bbls /month A R L
  • 12. Slop Oil & SourcesCalculationsA R L FLASH POINT CALCULATOR FLASH OF COMPONENT “SLOP" 38 C QUANTITY OF COMPONENT “SLOP" 75 BBLS FLASH OF COMPONENT "Blended HSD" 72 C QUANTITY OF COMPONENT "Blended HSD" 65 BBLS FLASH OF COMPONENT BLEND 54 C
  • 13. Slop Oil & Sources Main Sources : Units’ Sample Points Desalter/ JET Filters Drain Units’ start up Shut down Upsets at units Vacuum Creating System Main Sources DetailA R L
  • 14. Slop Oil & Sources Main Sources : Units’ Sample Points Desalter/ JET Filters Drain Units’ start up Shut down Upsets at units Vacuum Creating System Main Sources DetailA R L
  • 15. Slop Oil & Sources Main Sources : Units’ Sample Points Desalter/ JET Filters Drain Units’ start up Shut down Upsets at units Vacuum Creating System Main Sources DetailA R L
  • 16. OVER HEAD VESSEL TO SLOP TANK FOR RE-PROCESSING Sampling Testing Blending with HSD Vacuum Creating System Heavy Crude Unit (HCU) 1525 bbls / month A R L
  • 18. Slop Oil & SourcesSlop Oil Results Results of HCU Slop Oil From V-008 Sr. No RESULTS Sp. Gravity Color (ASTM) Flash Point ( C ) C.P ( C ) P. P (C ) 1 0.821 0.5 45 <-18 <-18 2 0.824 0.5 42 <-18 <-18 3 0.820 0.5 42 <-18 <-18 4 0.844 1.0 48 -9 -15 5 0.842 1.0 49 -9 -14 A R L
  • 19. Slop Oil & SourcesCalculationsA R L FLASH POINT CALCULATOR FLASH OF COMPONENT “SLOP" 48 C QUANTITY OF COMPONENT “SLOP" 1525 BBLS FLASH OF COMPONENT "Blended HSD" 72 C QUANTITY OF COMPONENT "Blended HSd" 550 BBLS FLASH OF COMPONENT BLEND 54 C
  • 20. HOT WELL STORAGE TANK LUMMUS SLOP REDUCTION 4210 bbls / month A R L
  • 22. Slop Oil & SourcesSlop Oil Results Results of Lummus Vacuum Separator / Tk-38 Sr. No RESULTS Sp. Gravity Color (ASTM) Flash Point ( C ) C.P ( C ) P. P (C ) 1 0.838 0.5 56 <-18 <-18 2 0.842 0.5 55 -15 -18 3 0.835 0.5 58 <-18 <-18 4 0.825 0.5 60 <-18 <-18 5 0.831 0.5 46 <-18 <-18 6 0.837 1.0 47 <-18 <-18 7 0.833 1.0 51 <-18 <-18 8 0.829 0.5 51 <-18 <-18 9 0.845 0.5 57 2 -9 A R L
  • 23. Slop Oil & SourcesCalculationsA R L FLASH POINT CALCULATOR FLASH OF COMPONENT “SLOP" 48 C QUANTITY OF COMPONENT “SLOP" 4210 BBLS FLASH OF COMPONENT "Blended HSD" 72 C QUANTITY OF COMPONENT "Blended HSD" 1400 BBLS FLASH OF COMPONENT BLEND 54 C
  • 24. Slop Oil & Sources Main Sources : Units’ Sample Points Desalter/ JET Filters Drain Units’ start up Shut down Upsets at units Vacuum Creating System Main Sources DetailA R L
  • 25. Achievements SLOP OIL RECOVERY DETAILS DETAILS SLOP OIL (TOTAL) SLOP OIL (Remaining) SLOP OIL (Recovered) HSD Required (for blending) TOTAL BLEND Lummus (VCS) 4210 0 4210 1400 5610 HCU (VCS) 1525 0 1525 550 2075 Jp-1 Filter Repacking 75 0 75 65 140 SAMPLING Points & Pump Drainages 3300 2750 550 170 720 TOTAL 9110 2750 6360 2185 8545 A R L
  • 26.  6360 bbls of Slop Oil recovered.  Reduction in SLOP OIL Re-Processing Cost reduced for 6360 bbls/month.  Blending of Recovered Oil with HSD, meeting Quality Standards.  One time profit of 6360 bbls excess HSD Production with out processing. A R L Achievements (cont.)
  • 27. NO QUESTIONS ??? A R L THANKS FOR ASKING