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Maximize Vacuum Residue Conversion and Processing Flexibility
with the UOP Uniflex™ Process
Hans Lefebvre UOP LLC, A Honeywell Company
© 2012 UOP LLC. All rights reserved.
XVIII Foro de Avances de la Industria de la Refinación
11 and 12, July, 2012 Mexico City, Mexico
UOP 5831-1
Impact of Global Crude Oil and Natural Gas Prices
150
120
100
90
60
0 Ga
s &
Oil
Pri
ce
($/M
MB
TU
)
Oil P
rice
($/B
BL
)
Natural gas price has not risen as quickly as crude oil
This favours upgrading because heavy fuel oil competes with gas, whereas transportation fuels are linked to crude oil price
This offers an increased residue conversion margin uplift
The widening differential favours “Hydrogen Addition”, rather than “Carbon Rejection”, due to:
− Increased product values
− Decreased H2 manufacturing costs
25
20
15
10
5
0 1990 1995 2000 2005 2010
Natural Gas
Crude Oil
25
20
15
10
5
0
1990 1995 2000 2005 2010
Delta
-5
$/M
MB
TU
Source: BP Statistical Review of World Energy 2011 UOP 5831-2
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
Pe
r D
ay
40
30
20
10
0 2000 2005 2010
Middle Distillates
Light Distillates
Heavy Fuel Oil
1995
Source: BP Statistical Review of World Energy 2011
UOP 5831-3
0
100
200
300
400
500
600
700
2000 2002 2004 2006 2008 2010
Mexico’s Oil Market
Pemex’s strategy is to reduce imports of gasoline and diesel by expanding capacity and increasing residue conversion capability
Dominant crude varieties in Mexico have high sulfur and high residue content
Addition of residue conversion with Delayed Coking increase a refineries yield of Naphtha + Diesel
High yield of Pet Coke
Th
ou
sa
nd
b
arr
els
Pe
r D
ay
Source: Pemex Statistical Yearbook 2011
Refined Product Imports into Mexico
Source: Business Plan of Petróleos Mexicanos
and Subsidiary Entities June 1, 2010
VGO
VGO VGO
Vacuum Residue
Vacuum Residue
Diesel Diesel Diesel
Naphtha
Naphtha
Naphtha Gas
Gas
Coke
Base Case Base Case+ FCC
Base Case+ FCC+ Coker
Benefits of Adding Conversion
UOP 5831-4
Gasoline + Diesel
Transportation Fuels:
Gasoline, Jet Fuel, Diesel
Dis
tilla
tio
n
Naphtha
Crude Oil
Vacuum Residue
Vacuum Gas Oil
Distillates
Residues: Heavy Fuel Oil,
Pitch, Coke
Naphtha Hydrotreating & Reforming
FCC or Hydrocracking
Distillate Hydrotreating
UOP’s Heavy Oil Upgrading Processes
Residue Conversion
UOP/FWUSA Solvent
Deasphalting
FWUSA SYDEC™
Delayed Coking Process
UOP/FWUSA Visbreaking
UOP RCD Unionfining™
Process
UOP Solutions for Residue Conversion
UOP Uniflex™
Process
UOP 5831-5
Uniflex Process Commercial Experience
Petro-Canada Montreal Unit 25 years R&D
15 years commercial operation
High conversion
Many UOP improvements in the last 5 years
-20
0
20
40
60
80
100
Yie
ld, vo
l %
Naphtha
Distillate
VGO
Pitch
85% 94% 90%
Commercial Performance Conversion
UOP 5831-6
Commercial Operations:
5000 BPD unit operated for 15 years in Montreal
Processed wide range of feedstocks
Excellent design correlations allowing accurate scale-up
Very high reliability / availability demonstrated (97+%)
Uniflex Process Commercial Experience
UOP Enhancements:
Completed UOP Schedule A design
Petro-Canada Montreal Unit with improvements
– Single train design: parallel reactors, common separation
– More efficient heat integration
– High conversion of HVGO
Integrated pilot plant matches with commercial performance
Analytical modeling supports optimization
UOP 5831-7
Uniflex Process Thermal Cracking of Asphaltenes
Heavier, higher sulfur feeds have higher reactivity
Wide boiling range containing olefins, aromatics, S, N
Further hydroprocessing is required
Archipelago Model of Asphaltenes, Carbon # = 313, MW = 4705
Source: M. Gray, Univ of Alberta
Benefits from a combination of:
1. Thermal cracking to shorter chain lengths
2. Catalyst inhibits coke through:
Hydrogenation of free radicals formed in thermal cracking
Physically hinders growth of coke precursors.
UOP 5831-8
Uniflex Process Reactor Achieves High Conversion
Feed, H2 and Catalyst
Products and Catalyst
Optimal design for high conversion
−Upflow
−High temperature and moderate pressure
Efficient utilization of reactor volume
−Low gas voidage
−High product vaporization
− Intense liquid backmixing
−Near isothermal
Asphaltene management
−Nano-scale dispersed catalyst
−Solubility control techniques
UOP 5831-9
Slurry Reactor
Vacuum Residue
HHPS
Stripper/ Fractionator
Naphtha
C4-
Catalyst
Recycle H2
Diesel
HVGO Recycle
Makeup H2
Vacuum Column
Uniflex Process with HVGO Recycle
Pitch
LVGO
CHPS
HVGO
Recycling Benefits:
HVGO is difficult to process in HT, HC and FCC units
Uniflex converts HVGO to valuable products
UOP 5831-10
UOP CONFIDENTIAL
Vacuum
Residue
UOP Uniflex
Simple Integration into Existing Refineries
Diesel Pool
Cru
de
& V
acu
um
D
isti
llati
on
Crude
Oil Vacuum
Gas Oil
Distillates
Existing Hydrocracking,
MHC or FCC
New Distillate Hydrotreating
-40
-20
0
20
40
60
80
100
Delayed Coking Uniflex
Vo
lum
e%
VGO VGO
Distillate Distillate
Naphtha
Naphtha
Coke
(Wt-%)
Pitch
(Wt-%)
Yield Comparison
Uniflex Integration Benefits
• >55% yield of diesel: 2x Delayed Coking
• Simple stand-alone hydrotreater produces
reformer feed and Euro V diesel
• ½ VGO yield of Delayed Coking often allows
VGO to be processed in existing units
UOP 5831-11
Maximizing Naphtha and Diesel in an FCC Refinery Basis: Maya Crude
VGO
VGO VGO VGO
Vacuum Residue
Vacuum Residue
Diesel Diesel Diesel
Diesel Naphtha
Naphtha
Naphtha
Naphtha
Gas
Gas
Gas
Pitch Coke
-60
-40
-20
0
20
40
60
80
100
Base Case Base Case+ FCC
Base Case+ FCC+ Coker
Base Case+ FCC+
Uniflex
Uniflex increases transportation fuel yields by 10 Wt-% when compared to the Coker case
Ind
ica
tive
Yie
lds
(W
t %
)
Hig
h V
alu
e P
rod
ucts
L
ow
V
alu
e F
uels
UOP 5831-12
Uniflex Benefits
So what else is new and different that makes the above even
more compelling? The answer is higher prevailing
crude oil prices
Commercially Proven
Low-value Feed
High Conversion
High-value Products
Step Change Margin Increase
UOP 5831-13
Uniflex Process Residue Upgrading Economics
The value-added margin is high – given low value feed and high value products
0.9
0.5
Product Revenue Cash Margin
VR H2
Cash
Operating Cost
Indicative Annual Cash Revenues / Costs ($ Billion)
Pitch
1.4
UOP 5831-14
Can be handled in: − Liquid form for nearby uses
− Solidified for offsite markets
End Uses include: − Cement Kilns
− Fluidized Bed Boilers
− Conventional Boilers
− Gasification
− Delayed Coking
Feed
Pitch Catalyst
Uniflex Process Pitch Product
UOP 5831-15
0
5
10
15
20
Global Average Gross Refining Margins 3 – 8 $/bbl over the last 20 years
GR
M (
$/b
bl
of
Cru
de
Oil
Pro
ce
ss
ed
)
3 – 8 $/bbl
~10 – 16
$/bbl
Indicative margin (GRM) after installation of a Uniflex
complex
Low-quality and low-value feed (typically Vacuum Residue)
High conversion to high quality products
1990 1995 2000 2005 2010
Uniflex complex DOUBLES your refinery margins
Source of Historical Global Indicator Margin (GIM): BP
UOP 5831-16
NRL in Pakistan to Construct 2nd Uniflex Unit
Distillate Unionfining
Uniflex
Vacu
um
D
isti
llati
on
Pitch to
Cement Plant
Atm
Resid
Unicracking
Naphtha & Diesel
Unconverted
Oil
Solvent Deasphalting
(Existing)
Vacuum
Resid
Lubes Stock
Lubes
SDA
Pitch
DA
O
VG
O
VGO
Naphtha
& Diesel
Lubes
Increases margins by $150 million/year
Distillate from Crude Lubes Extract
Vacuum
Resid
UOP 5831-17
Uniflex Benefits....
Uniflex is a highly compelling technology, maximizing the use of existing facilities to minimize capital cost, while offering a new commercially proven industry benchmark
in Residue Conversion
UOP 5831-18
The Time is Now: − Falling fuel oil demand
− Rising clean distillates demand
− High prevailing crude oil prices
− Low cost of hydrogen production
UOP 5831-19
Uniflex Benefits....
Uniflex is a highly compelling technology, maximizing the use of existing facilities to minimize capital cost, while offering a new commercially proven industry benchmark
in Residue Conversion
UOP 5831-20
The Time is Now: − Falling fuel oil demand
− Rising clean distillates demand
− High prevailing crude oil prices
− Low cost of hydrogen production