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Maximise Residue Conversion Economics with UOP
Bottom-of-the-Barrel Technologies
Maximise Residue Conversion Economics with UOP
Bottom-of-the-Barrel Technologies
Soumendra Banerjee (UOP India Pvt Ltd)Phil Hunt (UOP Ltd, UK)
UOP LLC, A Honeywell Company
Soumendra Banerjee (UOP India Pvt Ltd)Phil Hunt (UOP Ltd, UK)
UOP LLC, A Honeywell Company
© 2012 UOP LLC. All rights reserved.
PetroFedInternational Conference on Refining Challenges & Way Forward April 16th -17th 2012, New Delhi, India
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We Will Cover Five Related Topics
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� Why India and Why Now?
� Outline of Process Offering
� Integration Opportunities
� Key Economics Drivers
� Benefits & Opportunities
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2
3
4
5
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UOP UniflexTM Process is Ideal for the Indian Market
� State of the Indian Market− Is the 4th largest oil consumer (after USA, China and Japan)
− The rise in international crude oil prices in recent years has created major challenges for India, given the high reliance on imports, and has resulted in a need to maximize the utilization and conversion of crude oil processed in the country.
− The increased use of heavy crudes, distillate demand, particularly diesel, continues to show strong growth, and Indian refiners are being challenged to provide cleaner fuels to address concerns of air pollution and climate change.
− The cost advantage of heavy crudes over light crudes has incentivized many Indian refiners to process heavier crudes, therefore increasing the heavy residue produced at a time when fuel oil demand is declining.
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These is a strong need of residue upgrading technologiesthat maximize transportation fuels
Let’s Start with the Fundamentals...
What is residue and why convert it?
Characteristics: Heavy, dirty, low value, limited uses
Properties: High MW, stable and carbon rich, hydrogen deficient
Composition: Saturates, aromatics, resins, asphaltenes
Impurities: Sulfur, nitrogen, heavy metals
Vacuum residue is lower value than fuel oil due to the need to use cutter stocks
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Crude Oil and Natural Gas Prices
150
100
50
0Ga
s &
Oil
Pri
ce
($
/MM
BT
U)
Oil P
rice
($/B
BL
)
� Natural gas price has not risen as quickly as crude oil
� This favours upgrading because HFO competes with gas, whereas transportation fuels are linked to crude oil price
� The widening differential favours “Hydrogen Addition,” rather than “Carbon Rejection,” due to:
− Increased product values
− Decreased H2 production costs
20
10
01990 1995 2000 2005 2010
Natural GasCrude Oil
20
10
0
1990 1995 2000 2005 2010
Delta
$/M
MB
TU
Source: BP Statistical Review of World Energy 2011 UOP 5782-5
1990 – 2010 History
By 2010 – fuel oil had declined to only 15%
In 1970, 80, 90 – fuel oil was 50, 40, 30% of distillates demand
By 2020 – fuel oil is likely to be only 10% of distillates demand
Global Oil Product Demand(Heavy Fuel Oil and Distillates)
Millio
n b
arr
els
Per
Day
40
30
20
10
02000 2005 2010
Middle DistillatesLight DistillatesHeavy Fuel Oil
1995
Source: BP Statistical Review of World Energy 2011
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Transport Fuels:Gasoline,Jet FuelDiesel
Distillation
Distillation
Naphtha
Crude Oil
Vacuum Residue
Vacuum Gas Oil
Distillates
Residues:Heavy Fuel Oil,
Pitch, Coke
NaphthaNaphthaHydrotreating Hydrotreating & Reforming& Reforming
FCC FCC ororHydrocrackingHydrocracking
DistillateDistillateHydrotreatingHydrotreating
UOP’s Heavy Oil Upgrading Processes
ResidueResidueConversionConversion
UOP/FWUSASolvent
Deasphalting
FWUSA SYDEC™Delayed Coking
Process
UOP/FWUSAVisbreaking
UOP RCDUnionfining™
Process
UOP Solutions for Residue Conversion
UOP Uniflex™Process
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The Uniflex Technology Offering is......
UNIFLEX UNIT(Wt-%)
100
15
50
15
Vacuum Residue Feed
Naphtha
Diesel
VGO
HDT
MHC & FCC or HCU
� 90% Conversion
� Maximum Diesel
� Minimum VGO
� VGO integration
� Once through Catalyst
� Similar scheme to Unicracking
� Product streams require further upgrading
CatalystH2
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UOP has nearly 100 Years of Technology Expertise
This experience has been utilized to bring to market a commercially proven residue slurry bed hydrocracking technology for licensing…
Significant resources committed to construct and operate the CANMET plant for several years and for the subsequent UOP Uniflex Process
enhancements
Excellent correlation across:
� CANMET commercial plant
� UOP pilot plants
� Scale-up models UOP “SCHEDULE A”
UnicrackingUnicrackingProcessProcess
UnionfiningUnionfiningProcessProcess
Technology Licensing
CANMET
UOP Pilot
Plants
Scale-up Models
� Yields
� Conversion
� Consumption (H2, Catalyst)
� Product qualities
Wide range of:
� Feedstocks
� Operating conditions
Comprehensive feedstock and operating data:
UniflexUniflexProcessProcess
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Process Configuration and Design
REACTOR
FEED HEATING
FRACTIONATION SEPARATION
HOT & COLD SEPARATORS
The Uniflex Process is very similar in scheme to VGO hydrocracking
FEED HEATING, REACTOR, SEPARATION and FRACTIONATION
Uniflex Process operates at a similar reactor pressure to VGO hydrocracking (140 barg) with make-up and recycle hydrogen
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Commercial Operations:
� 5,000 BPD unit operated for 15 years at Petro-Canada Montreal
� Developed excellent design correlations allowing accurate scale-up
� Very high reliability demonstrated
� Achieved 95% conversion
Uniflex ProcessCommercial Experience
UOP Enhancements:
� Completed UOP Schedule A design
� Reflects experience of Petro-Canada Montreal Unit with improvements
– Large single train designs – parallel reactors, common separation
– More efficient heat integration
– High conversion of HVGO
� Integrated pilot plant closely matches commercial performance
� Analytical, modeling development programs support optimization
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Uniflex ProcessThermal Cracking of Asphaltenes
� Heavier, higher sulfur feeds have higher reactivity
� Wide boiling range of products containing olefins, S, N
� Further hydroprocessing of the distillate products is required
Archipelago Model of Asphaltenes, Carbon # = 313, MW = 4705Source: M. Gray, Univ of Alberta
The process benefits from a combination of:
1. Thermal cracking to shorter chain lengths
2. Inhibiting formation of coke through:
Hydrogenation of free radicals formed in thermal cracking
Catalyst physically hinders mesophase coalescence
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Uniflex Process ReactorAchieves High Conversion
Feed, H2and Catalyst
Productsand Catalyst � Optimal design for high conversion
−Upflow
−High temperature and moderate pressure
� Efficient utilization of reactor volume
−Low gas voidage
−High product vaporization
−Near Isothermal
� Asphaltene management
− Inhibit formation of coke pre-cursors
Commercially proven Reactor design with minor scale-up.
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Catalyst & Pitch
� UOP global supply of catalyst
� Multiple manufacturing locations
� Simple logistics and storage
Catalyst
� Cement:
– Often the most attractive outlet option
� Boiler/Power:
– Conventional power plants
– CFB
� Solidification:
– Proven technology
– Facilitates transportation and storage
Pitch
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Uniflex Process Key Success Factors
So what else makes the above even more compelling - the answer is
high crude oil prices
Commercially Proven
Low Value Feed
High Conversion
High Quality Products
Step Change Margin Increase
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Uniflex Complex Scope
Gasoline & Diesel
VGO
Distillates
HCUor
MHC/FCC
DHT
Uniflex Process Integration Benefits
• >55% yield of diesel: 2x Delayed Coking
• Stand-alone hydrotreater produces reformer feed and Euro V diesel
• ½ VGO yield of Delayed Coking enables processing in existing units
UniflexUniflexUnit
VR
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VGOVGOVGOVGO
DistillateDistillateDistillateDistillate
NaphthaNaphtha
NaphthaNaphtha
CokeCoke((WtWt--%)%)
Pitch (Pitch (WtWt--%)%)
Yield Comparison
100
80
60
40
20
0
-20
-40
Vo
lum
e %
Delayed Coking Uniflex Unit
The value-add margin is high – given low value feed and high value products
0.9
0.4
Product Revenue Cash Margin
VR H2
Cash Operating Cost
Indicative Annual Cash Revenues / Costs ($ Billion)
Pitch
1.3
An important cost parameter is the alternative value of feedstock
Uniflex Complex Indicative Upgrading Economics
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Uniflex Complex Indicative Upgrading Economics
Uniflex cases typically offer around a two times uplift in refinery margin, under typical pricing scenarios
0.9
Existing Refinery With Uniflex Project
UniflexCase
Refinery Margin ($/BBL)
UpliftUplift
1.4
MarginMargin
Typically Typically Doubling Doubling
the the MarginMargin
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Recent Uniflex Award Announcement....
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UOP LLC, a Honeywell company, recently announced that its new process technology designed to help refiners get more high-value product from each barrel of crude oil has been selected by an Asian refiner.
The facility, which is scheduled for start-up in 2016, will use Uniflex technology to upgrade its heavy residue into high-value distillate products. Of particular value to the refinery is the high yield of diesel from the Uniflex technology, which is nearly double that of competing residue conversion technologies.
The technology will be integrated with UOP Unionfining hydroprocessing solutions to process distillates into high-quality diesel fuel and naphtha into high-quality feedstock used for gasoline production.
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2
3
20 40 600
Average Carbon Number (Atoms per Molecule)
Hyd
rog
en
to
Ca
rbo
n A
tom
ic R
ati
o
DIESELDIESEL
VAC RESIDVAC RESID
COKE
Thermal Cracking
� Converting Vacuum Residue into Diesel requires:
− Thermal Cracking
and
− Hydrogenation
− Inhibiting Coke formation
� Uniflex Process achieves all the above:
− In a single slurry bed reactor
− With post treatment to meet finished product quality specifications
Uniflex Process Attributes Recap
Hydrogenation
CRUDEOIL
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Uniflex Process
Summary of the Uniflex Technology Offering
Uniflex Process is...
...a very flexible residue upgrading “Technology Solution”
...offering a step change (improvement) in refining margin
The key global market drivers for refiners are now aligned in support of residue upgrading – falling fuel oil demand, rising clean distillates
demand and high prevailing crude oil prices
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Uniflex Uniflex Technology is a highly Technology is a highly compelling process, that is compelling process, that is
commercially proven, offering commercially proven, offering maximum use maximum use of existing of existing facilities, facilities, and a new industry benchmark in and a new industry benchmark in
““zero zero fuel fuel oil” refiningoil” refining
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Uniflex Process
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