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Industrial Training at
Petromax Refinery Limited
| Presented by:
Pranto Paul (1402002)
Galib Hassan Khan (1402010)
ASM Nasim (1402015)
Tarikul Islam (1402019)
Arkabur Rahman Arnob (1402020)
Ahosan Habib Rakib (1402047)
Company Type: Privately Owned
Parent Company: Youth Group
Employees: around 250
Process Licensor: AXENS (France)
General Contractor: PT Istana Karang Laut, Indonesia
Local Contractor: SIGMA
Location:
Mongla Industrial Area, Khulna,
Bangladesh
(On the bank of the river Poshur)
Overview
Image Credit: Google Earth
Normal capacity: 2500 BPSD
Condensate Fractionation Unit (CFU)
Catalytic Reformation Unit (CRU)
Naphtha Hydrotreating (NHT)
Running Time: 24 hours
Raw Materials: Natural Gas Condensate
Main Products:
• Light Naphtha
• Premium grade Gasoline (Octane)
• Mineral Turpentine (MTT)
• Superior Kerosene Oil (SKO)
• Diesel
Major Process Units:
Process Overview
Condensate Fractionation Unit (CFU)
A Distillation column with 47 Equilibrium trays
Feed: Natural Gas Condensate
Output:
• Light Naphtha (Overhead)
• Naphtha (Overhead)
• Mineral Turpentine (Middle section)
• Superior Kerosene Oil (Middle Section)
• High Speed Diesel (Bottom)
• Preheating
• Re-boiling
• Condensation
• Stripping
Processes Involved:
Goes to NHT and
CRU for processing
Condensate Fractionation Unit (CFU)
ImageCredit:PetromaxRefineryLimited
Naphtha Hydrotreating (NHT)
Capacity: 6350 kg/hr
Feed: Naphtha from CFU
Purpose: To remove impurities from
Naphtha to make it suitable for CRU
Impurities Removed:
• Sulfur : Mercaptan, Sulfide (max 0.5 ppm)
• Water (max 4 ppm)
• Nitrogen (max 0.5 ppm)
• Oxygen
• Metallic compound : As, Fe, Pb, Cu etc. (max 5 ppb)
Reactions Involved:
• Hydrorefining (desulfurization)
• Hydrogenation
Catalysts Used:
• Bimetallic catalyst
• Cobalt-Molybdenum
• Used for the desulfurization and
denitrification
Distillation range: ASTM 80-180˚C
Naphtha Hydrotreating (NHT)
ImageCredit:PetromaxRefineryLimited
Catalytic Reformation Unit (CRU)
Purpose:
• To convert low octane naphtha to high
octane reformate product
• To produce high purity H2 for Hydro-treating
unit. Catalysts Used:
• Bimetallic catalyst
• Platinum & Rhenium.
• Total Catalyst of 3 Reactor: 6401 kg
Reactions Involved:
• Dehydrogenation
• Dehydrocyclisation
• Isomarization
• Cracking
• Hydrogenolysis
• Coking
Desired
Adverse
Feed: Naphtha from NHT
Output:
High Octane Blending Component (HOBC)
Catalytic Reformation Unit (CRU)
ImageCredit:PetromaxRefineryLimited
CFU
(Distillation)
NHT
(Impurity
removal)
CRU
(Increase of
Octane
number)
Tank Tank
Naphtha
MTT, SKO, HSD in
separate lines
NGC
feed
High Octane
naphtha
Process in short
Pre-treatment
Media-filtration
Softening by base
exchange
Demineralization
by Reverse
Osmosis
Polishing by ion-
exchange process
Water Treatment Plant
Water in Surrounding area is very salty
Controlling Parameters
✓ pH
✓ M-alkalinity
✓ Ca-Hardness
✓ Total Hardness
✓ Total Dissolved Solid
(TDS)
✓ Temperature
➢ Multi-grade Filter (MGF)
➢ Activated Carbon Filter (ACF)
➢ Softener
➢ Reverse Osmosis
➢ De-gasifier
➢ Ion Exchanger
Cation exchanger Anion exchanger
Water Treatment Plant units
Image Credit: Petromax Refinery Limited
Safety and Firefighting
Image Credit: Petromax Refinery Limited
Highly Flammable Substance: Oil
Sensor Cable
Signal
Tank Fire
Detection Panel
SIS/F&G
Panel
Foam Pump(s)
Controller
Deluge Valve for
Specific Tank
Sounder and Beacon
for Specific Zone
Auto Start
Jockey pump,
Elec. Fire Pump
& Diesel fire
pump System
Water
Pressure
Drop
Pump types for fire fighting
• Jockey pump :
Cut in: 142 psi
Cut out: 150 psi
• Electric Fire pump:
Cut in: 136 psi
Cut out: 148 psi
• Diesel Fire Pump:
Cut in: 120 psi
Cut out: 144 psi
Safety and Firefighting
The whole plant area is divided into 6 fire zones
Safety and Firefighting
Image Credit: Petromax Refinery Limited
• All the Toxic and hazardous gases are
burned in presence of Oxygen
• A burning Flare signals that the plant is
running
Flare
Thanks
for
your time

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Presentation on Industrial Training at Petromax Refinery Limited | 2018 | Chemical Engineering | BUET

  • 1. Industrial Training at Petromax Refinery Limited | Presented by: Pranto Paul (1402002) Galib Hassan Khan (1402010) ASM Nasim (1402015) Tarikul Islam (1402019) Arkabur Rahman Arnob (1402020) Ahosan Habib Rakib (1402047)
  • 2. Company Type: Privately Owned Parent Company: Youth Group Employees: around 250 Process Licensor: AXENS (France) General Contractor: PT Istana Karang Laut, Indonesia Local Contractor: SIGMA Location: Mongla Industrial Area, Khulna, Bangladesh (On the bank of the river Poshur) Overview Image Credit: Google Earth
  • 3. Normal capacity: 2500 BPSD Condensate Fractionation Unit (CFU) Catalytic Reformation Unit (CRU) Naphtha Hydrotreating (NHT) Running Time: 24 hours Raw Materials: Natural Gas Condensate Main Products: • Light Naphtha • Premium grade Gasoline (Octane) • Mineral Turpentine (MTT) • Superior Kerosene Oil (SKO) • Diesel Major Process Units: Process Overview
  • 4. Condensate Fractionation Unit (CFU) A Distillation column with 47 Equilibrium trays Feed: Natural Gas Condensate Output: • Light Naphtha (Overhead) • Naphtha (Overhead) • Mineral Turpentine (Middle section) • Superior Kerosene Oil (Middle Section) • High Speed Diesel (Bottom) • Preheating • Re-boiling • Condensation • Stripping Processes Involved: Goes to NHT and CRU for processing
  • 5. Condensate Fractionation Unit (CFU) ImageCredit:PetromaxRefineryLimited
  • 6. Naphtha Hydrotreating (NHT) Capacity: 6350 kg/hr Feed: Naphtha from CFU Purpose: To remove impurities from Naphtha to make it suitable for CRU Impurities Removed: • Sulfur : Mercaptan, Sulfide (max 0.5 ppm) • Water (max 4 ppm) • Nitrogen (max 0.5 ppm) • Oxygen • Metallic compound : As, Fe, Pb, Cu etc. (max 5 ppb) Reactions Involved: • Hydrorefining (desulfurization) • Hydrogenation Catalysts Used: • Bimetallic catalyst • Cobalt-Molybdenum • Used for the desulfurization and denitrification Distillation range: ASTM 80-180˚C
  • 8. Catalytic Reformation Unit (CRU) Purpose: • To convert low octane naphtha to high octane reformate product • To produce high purity H2 for Hydro-treating unit. Catalysts Used: • Bimetallic catalyst • Platinum & Rhenium. • Total Catalyst of 3 Reactor: 6401 kg Reactions Involved: • Dehydrogenation • Dehydrocyclisation • Isomarization • Cracking • Hydrogenolysis • Coking Desired Adverse Feed: Naphtha from NHT Output: High Octane Blending Component (HOBC)
  • 9. Catalytic Reformation Unit (CRU) ImageCredit:PetromaxRefineryLimited
  • 10. CFU (Distillation) NHT (Impurity removal) CRU (Increase of Octane number) Tank Tank Naphtha MTT, SKO, HSD in separate lines NGC feed High Octane naphtha Process in short
  • 11. Pre-treatment Media-filtration Softening by base exchange Demineralization by Reverse Osmosis Polishing by ion- exchange process Water Treatment Plant Water in Surrounding area is very salty Controlling Parameters ✓ pH ✓ M-alkalinity ✓ Ca-Hardness ✓ Total Hardness ✓ Total Dissolved Solid (TDS) ✓ Temperature
  • 12. ➢ Multi-grade Filter (MGF) ➢ Activated Carbon Filter (ACF) ➢ Softener ➢ Reverse Osmosis ➢ De-gasifier ➢ Ion Exchanger Cation exchanger Anion exchanger Water Treatment Plant units Image Credit: Petromax Refinery Limited
  • 13. Safety and Firefighting Image Credit: Petromax Refinery Limited Highly Flammable Substance: Oil
  • 14. Sensor Cable Signal Tank Fire Detection Panel SIS/F&G Panel Foam Pump(s) Controller Deluge Valve for Specific Tank Sounder and Beacon for Specific Zone Auto Start Jockey pump, Elec. Fire Pump & Diesel fire pump System Water Pressure Drop Pump types for fire fighting • Jockey pump : Cut in: 142 psi Cut out: 150 psi • Electric Fire pump: Cut in: 136 psi Cut out: 148 psi • Diesel Fire Pump: Cut in: 120 psi Cut out: 144 psi Safety and Firefighting
  • 15. The whole plant area is divided into 6 fire zones Safety and Firefighting Image Credit: Petromax Refinery Limited
  • 16. • All the Toxic and hazardous gases are burned in presence of Oxygen • A burning Flare signals that the plant is running Flare