axens marketable solution from residue to final products...
TRANSCRIPT
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Alexandre Javidi
Axens Marketable Solution from Residue to Final Products
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Market driver for Residue Conversion
H-Oil effluent upgrading possibilities (Iranian Heavy
Vacuum Residue)
Iranian Light Case Study
Synopsis
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Iranian Market Petroleum Products
Fuel oil Fuel oil
Middle Distillate
Middle Distillate
Gasoline Gasoline
Naphtha Naphtha LPG LPG
Other*
Other*
0.0
0.5
1.0
1.5
2.0
2.5
2016 2025
Iranian Market Demand
Other* = Refinery Gas, Ethane, Aviation Gasoline, Jet Gasoline, Kerosene (except Jet Kerosene), Petroleum Coke, Crude Oil etc,
NGL, Non Crude (Orimulsion etc), Lubricants, Bitumen, Paraffin Wax, Other Oil, Refinery Losses
Mbpd
Naphtha, Gasoline
Middle Distillate
Fuel Oil
Iranian Market Demand
2016-2025
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Fuel Oil Iranian market
50% is used for power generation
Gas is more and more used and replaces fuel oil for power
generation
• Largely available
• Better for environment
Fuel Oil that is not consumed in Iran is exported mainly to Asia
Possibility to increase profitability by making more
valuable products
Fuel Oil Market
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2016 Decision by International
Maritime Organization (IMO): global
switch in 2020 to 0.5 % Sulfur (from
currently 3.5 % High Sulfur Fuel Oil
(HSFO))
ECA’s (Emission Controlled Areas):
S specification remains at 0.1 %
In 2020, demand for HSFO will
strongly decrease worldwide
Source: IMO
2020: Sulfur Specification Decrease in Bunker Fuels
Focus on Marine Bunker Fuels Global Impact of 2020 Spec Change
0.1%
Need for Residue Desulfurization and Conversion
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Conversion Options Overall scheme from VR to on Spec Products
VR Low sulfur
Naphtha
Euro V Diesel
H-Oil
FLUID CATALYTIC
CRACKING BLOC
VGO
HYDROCRACKING
High octane
Gasoline (10 ppm)
PRODUCTS
DIESEL HDT *
Naphtha
LCO
1st Step 2nd Step
Conversion Step Polishing Step
Naphtha HDT
Diesel
VGO
RESIDUE UPGRADING SOLUTION
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Conversion Options Overall scheme from VR to on Spec Products
VR
H-Oil
FLUID CATALYTIC
CRACKING BLOC
VGO
HYDROCRACKING
PRODUCTS
DIESEL HDT *
Naphtha
LCO
1st Step 2nd Step
Conversion Step Polishing Step
Naphtha HDT
RESIDUE
UPGRADING
SOLUTION
Diesel
VGO
Low sulfur
Naphtha
Euro V Diesel
High octane
Gasoline (10 ppm)
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Case study : Conversion Options Overall scheme
VR
H-Oil
FLUID CATALYTIC
CRACKING BLOC
VGO
HYDROCRACKING
PRODUCTS
DIESEL HDT *
Naphtha
LCO
1st Step 2nd Step
Conversion Step Polishing Step
Naphtha HDT
RESIDUE
UPGRADING
SOLUTION
Diesel
GASOLINE oriented DIESEL oriented
Low sulfur
Naphtha
Euro V Diesel
High octane
Gasoline (10 ppm)
VGO
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Conversion Options- Gasoline oriented Overall scheme
VR
H-Oil
FLUID CATALYTIC
CRACKING BLOC
PRODUCTS
DIESEL HDT *
Naphtha
LCO
1st Step 2nd Step
Conversion Step Polishing Step
Naphtha HDT
RESIDUE
UPGRADING
SOLUTION
Diesel
GASOLINE oriented
Low sulfur
Naphtha
Euro V Diesel
High octane
Gasoline (10 ppm)
VGO
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Conversion Options- Diesel oriented Overall scheme
VR
H-Oil
VGO
HYDROCRACKING
PRODUCTS
DIESEL HDT *
Naphtha
1st Step 2nd Step
Conversion Step Polishing Step
Naphtha HDT
Diesel
DIESEL oriented
Low sulfur
Naphtha
Euro V Diesel
Lube VGO
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Conversion Options- Diesel oriented- H-Oil+ Overall scheme
VR
V
G
O
H-Oil
VGO
HYDROCRACKING
PRODUCTS
DIESEL HDT *
Naphtha
LCO
1st Step 2nd Step
Conversion Step Polishing Step
Naphtha HDT
Diesel
SDA
Pitch
DIESEL oriented
Low sulfur
Naphtha
Euro V Diesel
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VR
540+ Propeties
Iranian
Heavy
Blend
Spgr 1.066
Sulfur wt% 4.20
Nitrogen, ppmwt 6700
Ni+V, ppmwt 520
CCR, wt% 24.6
C7 asph. wt% 15
Vacuum Residue Properties
• Feed capacity: 50 000 BPSD
AT
VT
VR
540+
AR
360+ 50,000
BPSD
Iranian Heavy Blend
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Conversion Options H-Oil Iranian Heavy Case
VR
VGO
Low sulfur
Naphtha
Euro V Diesel
VGO
HSFO
H-Oil
FLUID CATALYTIC
CRACKING BLOC
VGO
HYDROCRACKING
High octane
Gasoline (10 ppm)
PRODUCTS
DIESEL HDT *
Naphtha
LCO
1st Step 2nd Step
C3=
Conversion Step 77 wt% Polishing Step
Naphtha HDT
RESIDUE
UPGRADING
SOLUTION
Diesel
UCO
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Conversion Options Overall scheme from VR to on Spec Products
VR
V
G
O
H-Oil
FLUID CATALYTIC
CRACKING BLOC
VGO
HYDROCRACKING
PRODUCTS
DIESEL HDT *
Naphtha
LCO
1st Step 2nd Step
Conversion Step Polishing Step
Naphtha HDT
RESIDUE
UPGRADING
SOLUTION
Diesel
Low sulfur
Naphtha
Euro V Diesel
High octane
Gasoline (10 ppm)
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Naphtha from H-Oil
• High Nitrogen, after HDT, can be sent to
Reforming
• Paraffinic naphtha, RON to be increased in
reforming
• Reduced Yields in comparison with SR
Naphtha:
› Typically, Naphtha from H-Oil < 10% of SR Naphtha
Naphtha Processing
Gas
Naphtha
Diesel
VGO
VR
H-Oil®
VR
Diesel HDT
Steam
Cracker
NHT Naphtha
Block Gasoline Pool
Olefins to Petro
1st Step 2nd Step
Naphtha properties
on Iranian Heavy
Spgr 0.715
S wt% 0.041
N wt ppm 40
RON 48
MON 47
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Diesel Properties
Diesel Processing
Gas
Naphtha
Diesel VGO
VR
H-Oil®
VR
Diesel HDT
ULSD + Cetane boost
Diesel HDT
ULSD Euro V Diesel
Diesel From H-Oil Euro V Spec
Sulphur, ppwt 1883 10 Max
Nitrogen, ppwt 1365 NA
Density 0.850 0.820- 0.845
Total Aromatics,
%wt 35-40 No spec
Cetane Index
D4737 44 46
Cetane Number
D613 40-45 51
1st Step 2nd Step
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Diesel from H-Oil Analyses
GC-2D SR Diesel Hoil Diesel
Sulphide/Thiophene 27% 5%
BT 54% 24%
DBT 18% 58%
Ph-T, BNT 0% 12%
Total Sulphur, ppmwt 8892 1835
Basic Nitrogen SR Diesel Hoil Diesel
Aniline 0% 2%
Quinoleine 27% 43%
acridine 13% 11%
Total Basic 41% 56%
Total Nitrogen, ppmwt 114 1832
Diesel from H-Oil
• Refractive Sulfur,
• High Basic Nitrogen (HDS/ H DA inhibitor)
• Heavy feed : high proportion of Mono Aromatics and Condensed Aromatics
SR Diesel
SR Diesel
H-Oil Diesel
H-Oil Diesel
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VGO from H-Oil
VGO Processing
Gas
Naphtha
Diesel
VGO
VR
H-Oil®
VR
Export
VGO HDT / HCK
FCC
Typical Values VGO from H-Oil
Sulphur, %wt 1.09
Nitrogen, ppwt 7200
Metals, Ni+V, ppwt <1
Hydrogen, %wt 11.4 - 12.2
Bunker Fuel
FCC67%
VGO HDT/HCK
33%
All Axens references VGO Processing
On specification products
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SR VGO HOil VGO
GC
xG
C-H
T
FT-I
CR
-MS
Zoom on aromatic area
More polyaromatics in H-Oil feed
More aromatic basic nitrogen molecules in H-Oil feed
VGO Feed Characterization
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UCO from H-Oil
UCO Processing
Gas
Naphtha
Diesel
VGO
VR
H-Oil®
VR
Coker
Gasification
Fuel
Bitumen
VR Export
SDA
Additional
Conversion
Additional
Conversion
By Blending
By Blending UCO from H-Oil Ratio VR Feed
Sulphur, ppwt 2.38 Lower
Nitrogen,
wt %
1.03 higher
Density 1.096 Higher
Metals, Ni+V,
ppwt
215 Lower
CCR, %wt 39 Higher
Hydrogen
Production
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Large panel of specification for Bunker Fuel or Fuel Oil
• Sulphur
• Density
• Viscosity at 50C
• Sediment / Stability
UCO Processing – Fuel Oil
H-Oil®
VR
Fuel
Worldwide Residual Fuel Oil Uses
2012
Thanks to FCC Slurry, LCO dilution, UCO is compliant with Fuel Market
Mix Bunker fuel and HSFO production
Options with FCC slurry and LCO
Production Bunker
Fuel Oil 60%
Production HSFO 40%
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VGO from H-Oil and DAO from SDA
UCO Processing Through SDA
Gas
Naphtha
Diesel
VGO
VR
H-Oil®
VR
Export
VGO HDT / HCK
FCC
DAO SDA
Typical Values VGO from H-Oil DAO from H-Oil + SDA
Sulphur, %wt 1.09 0.8 – 1.7
Nitrogen, ppwt 7200 1,600 -3,000
Metals, Ni+V, ppwt <1 C4 Solvent <3.5
Hydrogen, %wt 11.4 - 12.2 11.0 – 12.4
Pitch
Bunker Fuel
FCC67%
VGO HDT/HCK
33%
All Axens references VGO Processing
On specification products
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Wide range for Bitumen Specifications
+ local specifications
UCO / Pitch As Bitumen
H-Oil®
VR
SDA
Example of Bitumen quality Crude 1 Arabian /
US
Canadian
Heavy Crude
VR From H-Oil Yes Yes Yes in blend
VR from H-Oil + SDA pitch Yes No NA
After blowing treatment Yes yes NA
VR quality depends on:
• Crude origin
• H-Oil conversion
• Operation SDA
UCO to Bitumen has been validated without dilution requirement
Bitumen could be an alternate destination to increase refinery margins
Main Bitumen Specification – European Market
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Conventional Boilers for Steam Production
• Limited by Feed viscosity max 40cst @ 100°C
Mitsubishi technology solution
• Pulverised Fire Boiler operating at high temperature
• Steam Production and / or Electical Power
• Advantages :
› Fouling Resistant
› Technology proven on similar services (SDA Pitch)
UCO/Pitch to Boiler
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Two options:
• Solid Feed slurry of pitch + water sent to gasification
requires intermediate granulation
• Liquid Feed on-line pitch or UCO product sent to gasification unit
No issue for pelletisation, storage and transportation
Preferred option
In both cases, several schemes possible • Co-production of CO+H2 and steam
• Production of electricity (IGCC): Gasification + gas turbine + steam turbine
UCO/Pitch to Gasification
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Gasification of UCO From H-Oil / pitch directly from the SDA
MPG technology from Lurgi is the most suitable one for oil-base streams.
• No limitations on Flash Point of Feedstock
• Viscosity up to 300 cst
• Long burner life time result in higher reliability
and availability of plant
UCO/Pitch to Gasification
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Final Product Slates
10% 21% 22%
52% 41%
59%
21%
17%
23% 11%
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
Diesel oriented Gasoline oriented Diesel oriented with SDA
Iranian Heavy Case
Sweet Fuel Gas
LPG
High octane gasoline
Low sulfur Naphtha
euro V dieseil
Fuel
Pitch
9% 18% 20%
58% 44%
64%
18%
11%
19% 11%
0%
20%
40%
60%
80%
100%
Diesel oriented Gasoline oriented Diesel oriented with SDA
Iranian Light case
Sweet Fuel Gas
LPG
High octane gasoline
Low sulfur Naphtha
euro V dieseil
Fuel
Pitch
Product Slates on VR from Iranian Heavy
Product Slates On VR from Iranian Light
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Conversion Options Feeds description
AT
VT
Iranian Light crude
VR
540+
Light Iranian VR
555+
Sulfur wt% 4.12
Nitrogen, ppmwt 2600
Ni+V, ppmwt 92
CCR, wt% 23.7
C7 asph. wt% 6.4
Heavy Iranian VR
540+
Sulfur wt% 4.2
Nitrogen 6700
Ni+V 520
CCR 24
C7 asph. wt% 15
Iranian Heavy crude
AR
360+
AT
VT
VR
540+
AR
360+
50,000
BPSD 50,000
BPSD
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Conversion Options Feeds description
AT
VT
Iranian Light crude
VR
540+
Light Iranian VR
555+
Sulfur wt% 4.12
Nitrogen, ppmwt 2600
Ni+V, ppmwt 92
CCR, wt% 23.7
C7 asph. wt% 6.4
Heavy Iranian VR
540+
Sulfur wt% 4.2
Nitrogen 7000
Ni+V 520
CCR 24
C7 asph. wt% 15
Iranian Heavy crude
AR
360+
AT
VT
VR
540+
AR
360+
50,000
BPSD 50,000
BPSD
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Conversion Options H-Yields on Iranian Light VR
VR
Low sulfur
Naphtha
Euro V Diesel
VGO
HSFO
H-Oil
FLUID CATALYTIC
CRACKING BLOC
VGO
HYDROCRACKING
High octane
Gasoline (10 ppm)
PRODUCTS
DIESEL HDT *
Naphtha
LCO
1st Step 2nd Step
C3= Conversion Step : 80% wt Polishing Step
Naphtha HDT
RESIDUE
UPGRADING
SOLUTION
Diesel
UCO 17
33
33
9
5
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
Wt % Yields
UCO VGO Diesel Naphtha Light end
VGO
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VGO Processing
Gas
Naphtha
Diesel
VGO
VR
H-Oil®
VR
Export
VGO HDT / HCK
FCC
Typical Values VGO from H-Oil
Sulphur, %wt 0.45
Nitrogen, ppwt 1529
Metals, Ni+V, ppwt <1
Hydrogen, %wt 11.4 - 12.2
Bunker Fuel On specification products
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Final Product Slates comparison
10% 21% 22%
52% 41%
59%
21%
17%
23% 11%
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
Diesel oriented Gasoline oriented Diesel oriented with SDA
Iranian Heavy Case
Sweet Fuel Gas
LPG
High octane gasoline
Low sulfur Naphtha
euro V dieseil
Fuel
Pitch
9% 18% 20%
58% 44%
64%
18%
11%
19% 11%
0%
20%
40%
60%
80%
100%
Diesel oriented Gasoline oriented Diesel oriented with SDA
Iranian Light case
Sweet Fuel Gas
LPG
High octane gasoline
Low sulfur Naphtha
euro V dieseil
Fuel
Pitch
Product Slates On VR from Iranian Heavy
Product Slates On VR from Iranian Light
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H-Oil® is part of whole conversion scheme and each
solution is unique and taylor made for a refiner
Axens is a unique licensor with all the technology to
provide the most competitive scheme for refinery market
demand
H-Oil technology permits :
• To lower your fuel oil production
• Reach high conversion with most competitive economics
Conclusion
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Thank you! And see you on Axens’ Blog
axens.net/blog