Diesel
Diesel
Gas Oil
Gas Oil
Crude Oil
Crude Oil
Bitumen
Bitumen
Roads
Long Chain Molecules
Long Chain Molecules
Gas treatment
Gas treatment
Sulphur
Sulphur
Recovery
Recovery Sulphur
Sulphur
H
H2
2S
S H
H2
2S
S
Waxy Distillate
Waxy Distillate
Butane
Butane
De-asphalting
De-asphalting
Asphalt
Asphalt Fuel oil
Fuel oil
De-asphalted oil DAO
De-asphalted oil DAO
Desulphurisation
Desulphurisation
Kerosine
Kerosine
Shorter Chain Molecules
Shorter Chain Molecules
Hydrogen
Hydrogen
Manufacturing
Manufacturing
Unit
Unit
Hyrdrocracker
Hyrdrocracker
Hydrogen
Hydrogen
High Vacuum
High Vacuum
Separation
Separation
Vacuum Gas Oil
Vacuum Gas Oil
Long Residue
Long Residue
Distillation
Distillation
Diagram of Refinery Units
Diagram of Refinery Units
Platformer
Platformer Petrol
Petrol
CDU1
CDU2
HVU1
BBU
HVU2
BDU
HCU
HMU
HDS2
Split
HDT
Plat
DePr
HDS1
Fuel
Gas
GasOil
Blend
Mogas
Blend
FuelOil
Blend
RG
RG
H2
RG
H2
RG
H2
RG
H2
RG
Natural Gas
Syngas and Reformates
Condensates and Low
Sulphur Crudes
High Sulphur Crudes
Imported Residues
High Sulphur Crudes
Low Sulphur Crudes
Imported Residues
Naphtha
Kero
LGO
HGO
Long Residue
Naphtha
Kero
LGO
HGO
Long Residue
Sulphur
Refinery Gas
Regular Mogas
Premium Mogas
Kero / Avtur
CO2
Automotive Gasoils
and Marine
Light Fuel Oil
Bunkers
Heavy Fuel Oil
Refinery Fuel
Bitumen 80/100
Bitumen 180/200
Bitumen 45/55
The Process Units
The Process Units
GASOILS
GASOILS
32%
32%
JET/ KERO
JET/ KERO
14%
14%
MOGAS
MOGAS
30%
30%
FUEL AND LOSS
FUEL AND LOSS
7%
7%
FUEL OILS
FUEL OILS
17%
17%
Approx 7 Barrels to the Tonne
Approx 7 Barrels to the Tonne
A Typical Crude Barrel
A Typical Crude Barrel
Distiller Units
Distiller Units
Platformer
Hydrocracker
Gasoil Hydrotreater
Kerosine Hydrodesulphuriser
Depropaniser
Hydrogen Manufacturing unit
High Vaccuum Unit
Butane Deasphalting unit
Bitumen Unit
Sulphur Recovery
Product Blending
Crude
Crude
Products out
Products out
The Process Units
The Process Units
Distillation
Distillation
• The initial separation takes place
The initial separation takes place
in the distillation Column
in the distillation Column
• The Crude is first heated in a furnace
The Crude is first heated in a furnace
to a temperature of 360
to a temperature of 360 o
o
C
C
• It enters the column and vapours and
It enters the column and vapours and
liquids separate
liquids separate
• The light vapours rise to the top whilst
The light vapours rise to the top whilst
the heavier liquids fall to the bottom
the heavier liquids fall to the bottom
Furnace
Furnace
Distillation Column
Distillation Column
Crude
Crude
Kerosene
Kerosene
Gases +Tops + Naphtha
Gases +Tops + Naphtha
Light Gasoil
Light Gasoil
Heavy Gasoil
Heavy Gasoil
Long Residue
Long Residue
Crude
Lower Boiling
Lower Boiling
Higher Boiling
Higher Boiling
Distillation Column
Distillation Column
Desulphurisation
Desulphurisation
Hydrogen
Hydrogen
Under Pressure and Heat
Under Pressure and Heat
Reaction takes place and
Reaction takes place and
Hydrogen bonds with
Hydrogen bonds with
Sulphur to form H
Sulphur to form H2
2s
s
Desulphurisation Process
Desulphurisation Process
Reactor
Reactor
Catalyst
Catalyst
Sour Tops + Naphtha
Sour Tops + Naphtha
Sour Gasoil
Sour Gasoil
Sour Kerosene
Sour Kerosene
Desulphurised Kerosene
Desulphurised Kerosene
Desulphurised Tops + Naphtha
Desulphurised Tops + Naphtha
Desulphurised Gasoil
Desulphurised Gasoil
H2S
H2S
• Increases low Octane Naphtha to high
Increases low Octane Naphtha to high
Octane Platformate
Octane Platformate
• Uses Heat and Pressure in a Reactor
Uses Heat and Pressure in a Reactor
• Hydrogen is evolved in the process
Hydrogen is evolved in the process
• Platinum Catalyst assists the process
Platinum Catalyst assists the process
PLATFORMING
PLATFORMING
PLATFORMING
PLATFORMING
Plat
Platinum Re
inum Reforming
forming
High Octane
High Octane
Platformate
Platformate
Naphtha
Naphtha
From Splitter
From Splitter
Hydrogen
Hydrogen
Recycle
Recycle
Hydrogen
Hydrogen
To Users
To Users
Reactor
Reactor
Furnace
Furnace
Separator
Separator
50 OCTANE
50 OCTANE
100 OCTANE
100 OCTANE
520°C
520°C
18 barg
18 barg
515°C
515°C
40°C
40°C
E
E
Platformer Unit
Platformer Unit
Blending Tank
Blending Tank
High Vacuum
High Vacuum
&
&
Bitumen Units
Bitumen Units
Bitumen Feed Tanks
Bitumen Feed Tanks
Long Residue
Long Residue
High Vacuum Unit - HVU 1
High Vacuum Unit - HVU 1
Vacuum
Vacuum
Gases
Gases
Vacuum
Vacuum
Gas Oil
Gas Oil
180 Pen
180 Pen
Bitumen
Bitumen
To Hydrocracker
To Hydrocracker
for furthur Processing
for furthur Processing
Gases
Gases
Vacuum
Vacuum
Gas Oil
Gas Oil
180 Pen
180 Pen
Bitumen
Bitumen
Blowing
Blowing
Column
Column
To Refinery Gas System
To Refinery Gas System
Truck Loading and shipping
Truck Loading and shipping
45/55 Pen
45/55 Pen
Bitumen
Bitumen
Hydrocracking
Hydrocracking
What is Hydrocracking ??
What is Hydrocracking ??
Production of
Production of high quality light products
high quality light products
from heavy oils,
from heavy oils,
in the presence of Hydrogen.
in the presence of Hydrogen.
Hydrocracker Overview
Hydrocracker Overview
HCU
Long Residue
5500 t/d
HVU VGO
200 t/d
3200 t/d
Waxy Distilate
BDU
Asphalt
900 t/d
Asphalt
10 t/d
70 t/d
Butane
145 t/d
Plant gas
Adip gas
Steam
1400 t/d
Hydrogen
140 t/d
Tops/Naphtha
Gasoil
Gas
120 t/d
1100 t/d
2000 t/d
900 t/d
Kerosine
Short Residue
1900 t/d
DAO
1000 t/d
Hydrogen
Manufacturing
Unit
Hydrocracker
Hydrocracker
High Vacuum Unit
High Vacuum Unit
BUTANE DE-ASPHALTING UNIT
BUTANE DE-ASPHALTING UNIT
Sulphur Recovery
Sulphur Recovery
Unit
Unit
Converts H
Converts H2
2S into Sulphur
S into Sulphur
For use by Fertiliser Companies
For use by Fertiliser Companies
Sulphur Pit
Sulphur Pit
H
H2
2S Feed
S Feed Main Furnace
Main Furnace
Coalescer
Coalescer
Stack
Stack
Line Burner
Line Burner
Incinerator
Incinerator
Reactor
Reactor
Reactor
Reactor
Waste Heat
Waste Heat
Boiler
Boiler
Line Burner
Line Burner
Fuel Gas
Fuel
Gas
Line Burner
Line Burner
Fuel Gas
Liquid Sulphur
Liquid Sulphur 59%
59%
A
A
A
A
B
B C
C
D
D
C
C
B
B D
D
Liquid Sulphur
Liquid Sulphur
Liquid Sulphur
Liquid Sulphur
Sulphur Recovery Unit
Sulphur Recovery Unit
ENVIRONMENTAL
ENVIRONMENTAL
LOWERS EMISSIONS
LOWERS EMISSIONS
SCOT Unit
SCOT Unit
Reactor
Reactor
Waste Heat Boiler
Waste Heat Boiler
Upper Quench Column
Upper Quench Column
To SWS
To SWS
Quench Water
Quench Water
Cooler
Cooler
Lower Quench Column
Lower Quench Column
Blower
Blower
KO
KO Drum
Drum
SCOT Feed Gas
SCOT Feed Gas
SCOT Burner
SCOT Burner
FG
FG
Air
Air
SCOT Unit
SCOT Unit
Absorber Colum (ADIP)
Absorber Colum (ADIP)
To SRU
To SRU
KO
KO Drum
Drum
Lean ADIP
Lean ADIP
Semi Rich ADIP
Semi Rich ADIP

Refining_Process Refining_Process Refining_Process.ppt

  • 1.
    Diesel Diesel Gas Oil Gas Oil CrudeOil Crude Oil Bitumen Bitumen Roads Long Chain Molecules Long Chain Molecules Gas treatment Gas treatment Sulphur Sulphur Recovery Recovery Sulphur Sulphur H H2 2S S H H2 2S S Waxy Distillate Waxy Distillate Butane Butane De-asphalting De-asphalting Asphalt Asphalt Fuel oil Fuel oil De-asphalted oil DAO De-asphalted oil DAO Desulphurisation Desulphurisation Kerosine Kerosine Shorter Chain Molecules Shorter Chain Molecules Hydrogen Hydrogen Manufacturing Manufacturing Unit Unit Hyrdrocracker Hyrdrocracker Hydrogen Hydrogen High Vacuum High Vacuum Separation Separation Vacuum Gas Oil Vacuum Gas Oil Long Residue Long Residue Distillation Distillation Diagram of Refinery Units Diagram of Refinery Units Platformer Platformer Petrol Petrol
  • 2.
    CDU1 CDU2 HVU1 BBU HVU2 BDU HCU HMU HDS2 Split HDT Plat DePr HDS1 Fuel Gas GasOil Blend Mogas Blend FuelOil Blend RG RG H2 RG H2 RG H2 RG H2 RG Natural Gas Syngas andReformates Condensates and Low Sulphur Crudes High Sulphur Crudes Imported Residues High Sulphur Crudes Low Sulphur Crudes Imported Residues Naphtha Kero LGO HGO Long Residue Naphtha Kero LGO HGO Long Residue Sulphur Refinery Gas Regular Mogas Premium Mogas Kero / Avtur CO2 Automotive Gasoils and Marine Light Fuel Oil Bunkers Heavy Fuel Oil Refinery Fuel Bitumen 80/100 Bitumen 180/200 Bitumen 45/55 The Process Units The Process Units
  • 3.
    GASOILS GASOILS 32% 32% JET/ KERO JET/ KERO 14% 14% MOGAS MOGAS 30% 30% FUELAND LOSS FUEL AND LOSS 7% 7% FUEL OILS FUEL OILS 17% 17% Approx 7 Barrels to the Tonne Approx 7 Barrels to the Tonne A Typical Crude Barrel A Typical Crude Barrel
  • 4.
    Distiller Units Distiller Units Platformer Hydrocracker GasoilHydrotreater Kerosine Hydrodesulphuriser Depropaniser Hydrogen Manufacturing unit High Vaccuum Unit Butane Deasphalting unit Bitumen Unit Sulphur Recovery Product Blending Crude Crude Products out Products out The Process Units The Process Units
  • 5.
    Distillation Distillation • The initialseparation takes place The initial separation takes place in the distillation Column in the distillation Column • The Crude is first heated in a furnace The Crude is first heated in a furnace to a temperature of 360 to a temperature of 360 o o C C • It enters the column and vapours and It enters the column and vapours and liquids separate liquids separate • The light vapours rise to the top whilst The light vapours rise to the top whilst the heavier liquids fall to the bottom the heavier liquids fall to the bottom
  • 6.
    Furnace Furnace Distillation Column Distillation Column Crude Crude Kerosene Kerosene Gases+Tops + Naphtha Gases +Tops + Naphtha Light Gasoil Light Gasoil Heavy Gasoil Heavy Gasoil Long Residue Long Residue
  • 7.
    Crude Lower Boiling Lower Boiling HigherBoiling Higher Boiling Distillation Column Distillation Column
  • 8.
  • 9.
    Hydrogen Hydrogen Under Pressure andHeat Under Pressure and Heat Reaction takes place and Reaction takes place and Hydrogen bonds with Hydrogen bonds with Sulphur to form H Sulphur to form H2 2s s Desulphurisation Process Desulphurisation Process Reactor Reactor Catalyst Catalyst Sour Tops + Naphtha Sour Tops + Naphtha Sour Gasoil Sour Gasoil Sour Kerosene Sour Kerosene Desulphurised Kerosene Desulphurised Kerosene Desulphurised Tops + Naphtha Desulphurised Tops + Naphtha Desulphurised Gasoil Desulphurised Gasoil H2S H2S
  • 10.
    • Increases lowOctane Naphtha to high Increases low Octane Naphtha to high Octane Platformate Octane Platformate • Uses Heat and Pressure in a Reactor Uses Heat and Pressure in a Reactor • Hydrogen is evolved in the process Hydrogen is evolved in the process • Platinum Catalyst assists the process Platinum Catalyst assists the process PLATFORMING PLATFORMING
  • 11.
  • 12.
    High Octane High Octane Platformate Platformate Naphtha Naphtha FromSplitter From Splitter Hydrogen Hydrogen Recycle Recycle Hydrogen Hydrogen To Users To Users Reactor Reactor Furnace Furnace Separator Separator 50 OCTANE 50 OCTANE 100 OCTANE 100 OCTANE 520°C 520°C 18 barg 18 barg 515°C 515°C 40°C 40°C E E Platformer Unit Platformer Unit Blending Tank Blending Tank
  • 13.
  • 14.
    Bitumen Feed Tanks BitumenFeed Tanks Long Residue Long Residue High Vacuum Unit - HVU 1 High Vacuum Unit - HVU 1 Vacuum Vacuum Gases Gases Vacuum Vacuum Gas Oil Gas Oil 180 Pen 180 Pen Bitumen Bitumen
  • 15.
    To Hydrocracker To Hydrocracker forfurthur Processing for furthur Processing Gases Gases Vacuum Vacuum Gas Oil Gas Oil 180 Pen 180 Pen Bitumen Bitumen Blowing Blowing Column Column To Refinery Gas System To Refinery Gas System Truck Loading and shipping Truck Loading and shipping 45/55 Pen 45/55 Pen Bitumen Bitumen
  • 16.
  • 17.
    What is Hydrocracking?? What is Hydrocracking ?? Production of Production of high quality light products high quality light products from heavy oils, from heavy oils, in the presence of Hydrogen. in the presence of Hydrogen.
  • 18.
    Hydrocracker Overview Hydrocracker Overview HCU LongResidue 5500 t/d HVU VGO 200 t/d 3200 t/d Waxy Distilate BDU Asphalt 900 t/d Asphalt 10 t/d 70 t/d Butane 145 t/d Plant gas Adip gas Steam 1400 t/d Hydrogen 140 t/d Tops/Naphtha Gasoil Gas 120 t/d 1100 t/d 2000 t/d 900 t/d Kerosine Short Residue 1900 t/d DAO 1000 t/d Hydrogen Manufacturing Unit Hydrocracker Hydrocracker High Vacuum Unit High Vacuum Unit BUTANE DE-ASPHALTING UNIT BUTANE DE-ASPHALTING UNIT
  • 19.
    Sulphur Recovery Sulphur Recovery Unit Unit ConvertsH Converts H2 2S into Sulphur S into Sulphur For use by Fertiliser Companies For use by Fertiliser Companies
  • 20.
    Sulphur Pit Sulphur Pit H H2 2SFeed S Feed Main Furnace Main Furnace Coalescer Coalescer Stack Stack Line Burner Line Burner Incinerator Incinerator Reactor Reactor Reactor Reactor Waste Heat Waste Heat Boiler Boiler Line Burner Line Burner Fuel Gas Fuel Gas Line Burner Line Burner Fuel Gas Liquid Sulphur Liquid Sulphur 59% 59% A A A A B B C C D D C C B B D D Liquid Sulphur Liquid Sulphur Liquid Sulphur Liquid Sulphur Sulphur Recovery Unit Sulphur Recovery Unit
  • 21.
  • 22.
    Reactor Reactor Waste Heat Boiler WasteHeat Boiler Upper Quench Column Upper Quench Column To SWS To SWS Quench Water Quench Water Cooler Cooler Lower Quench Column Lower Quench Column Blower Blower KO KO Drum Drum SCOT Feed Gas SCOT Feed Gas SCOT Burner SCOT Burner FG FG Air Air SCOT Unit SCOT Unit Absorber Colum (ADIP) Absorber Colum (ADIP) To SRU To SRU KO KO Drum Drum Lean ADIP Lean ADIP Semi Rich ADIP Semi Rich ADIP

Editor's Notes

  • #16 SLIDE 1. Hydro-cracking INTRODUCTION Basic presentation Interactive Ask Questions If anything is not understood - ask.
  • #17 SLIDE 2. Hydro-cracking What is Hydro-cracking?? Hydro-cracking is a process that UPGRADES heavy oil, into lighter oils, in a Hydrogen rich atmosphere. ------------------------------------ Produces high quality, light products from heavy oils, in the presence of hydrogen.
  • #18 SLIDE 9. HCU Overview We take this LONG RESIDUE, and pass it through a couple of downstream Units, to extract oils, that provide us with feed for the Hydro-Cracker Unit. One of these units is called a HIGH VACUUM UNIT and the other is called a BUTANE De-ASPHALTING UNIT. -------------------------------------------------------------- As has been already mentioned,the Hydro-cracking takes place in a HYDROGEN RICH ATMOSPHERE, so we need a supply of Hydrogen, of high quality and purity. This is provided by another unit called a HYDROGEN MANUFACTURING UNIT. Lets now have a look at these 3 Units in a bit more detail.