Cap. 11 Perspectiva de Proyectos P-R
Cap. 11 Perspectiva de Proyectos P-R
Cap. 11 Perspectiva de Proyectos P-R
August 2013
Content
Cd. Madero
• 190 Mbd
• Coker
Salamanca Minatitlán
• 245 Mbd • 185 Mbd
• FCC + Lubs • FCC - Coker
Tula
• 315 Mbd
• FCC Alk H-Oil
Salina Cruz
• 330 Mbd
• FCC Alk
(1) Tame, M. LI IMIQ National Meeting, Puebla, México. October, 2011
(2) Data for March, 2011
Crude Slate in Mexico
Light Isthmus
Crude Crude Production
Producción (1)
de Crudo (1)
33.1 oAPI
4000
3500
3000 925
Heavy Maya 946
1012
Ligero
1036
2500
M BPD
Total Reserves Crude
2000 1180
22.1 oAPI Pesado +
1500
2458 2387 2244
ExtraPesado
1000 2045
1404
500
Extra-Heavy
0
KMZ Crude
2004 2005 2006 2007 2010
12.2 oAPI
(1) Diagnóstico, Situación de Pemex, Pemex, Marzo de 2008, updated to January 2011
Content
28
22
20
14
2001 2002 2003 2004 2005 2006 2007 2008 2009 2010
9
Source: CAPEM, México, marzo 2010.
Mexico: Fuels Use by Sector, 2009
MMBPD
1.36
1.8
1.8 Crude Exports Distribution by Sector
120
%
100 5
4
Non-Energy
80 19 use
Crude Production Agriculture
AA Proceso
CrudeProceso
domestic
1.3 1.22 60
1.3
processing 27 Residential &
2.58
3.3
3.3 Public Use
1.22
Elaboración
Elaboración 40 Industry
1.3
1.3
Transportation
20 45
Sources: Balance Nacional de Energía, 2010, SENER, Anuario Estadístico Pemex. 2011
Supply/Demand Issues in Mexican Refining Structure
Current Capacity does not meet the demand needs and the
distribution network to the Central Mexico Area is saturated.
Imports
Gasoline
Gasoline 718 432
446
793
802
(MBPD 2010
MBPD 2009)
370
Exports
Fuel Oil
Fuel Oil
MBPD 2009)
(MBPD 2010 279 317
-38
Demand Supply Balance
AAGR, %
Real Pronóstico(1) 2000-2011 2011-2016
1,800
Gasoline
-0.26 6.94
1,600 Premium
1,400
Gasoline Premium Gasoline
1,200 Gasoline Regular 4.59 4.06
Regular
1,000
800 Jet Fuel 0.07 4.60
600 JetFuel
400 Diesel 2.90 3.04
Diesel
200 Fuel Oil
Fuel Oil -8.90 -6.20
0
2000 2001 2002 2003 2004 2005 2006 2007 2008 2009 2010 2011 2012 2013 2014 2015 2016
Supply Deficit of
the Domestic
Market and
surplus of Fuel Oil
Production
Gasoline Demand is
expected to keep
growing
Gasoline Consumption Rate increase in Mexico
1,200
Millones de Dólares/mes
7,000
Miles de Barriles por Día .
6,000
México The strategy
5,000
does not around the
4,000 Consumo
Demand world is to
3,000 Supply
Producción produce at
2,000 least the
1,000
fuels
consumed
0
by the
ita
ia
ia
a
a
na
n
o
l
a
si
domestic
ci
ad
el
pó
an
ic
d
d
ra
hi
an
In
u
éx
au
an
m
Ja
ez
Fr
M
le
S
market
C
en
A
a
V
bi
ra
A
% Growth
País 1995 2005 2010 (1995- 2010)
14%
Predicted
Imports 47%
Consumption
13%
Consumption
Production
M BPD
Year
MM USD/year
Cost of a New
300,000 BPD
Refinery
Year
Maximize
Value Added Corporate Social
Growth under Responsability
Sustainability
■ Take actions to face ■ To improve relationships with
the increasing refining customers and suppliers
products demand
■ Safety and Sustainability as key
■ Include Technology as Efficient drivers in Operations
a tool for creating Managemenet
competitive
advantages ■ Improve Business Processes
■ Increase managemenet empowerment
■ Speed up operational decision making
Pemex Strategies to Develop the Refining Industry
15 Average
Average 2006-2015 • Minatitlán Reconfiguration,
1995-2005 7.5 US$/b completed.
5.0 US$/b Refineries
10 Reconfiguration • Residual Conversion
projects (Delayed Coking)
at Salamanca and Salina
5 Heavy Maya Cruz.
Coker Scheme
Reduce Residual
3 2
production and increase Produce ULSG and ULSD
distillates yields
1
1
Crude Slate with 1 1 3 New Refining 1 3
3 Train at Tula 2
60% Heavy Crude Residual
in the National 250 MBPD
2 Conversion Project
Refining System Minatitlan Refinery + Residue Reconfiguration
at
Reconfiguration to Processing of the Salina
Production of Salamanca Cruz Refinery
process a Crude From the
ULS Fuels Refinery to process
Slate with 70% existing Tula
Vaccum residue
Heavy Crude Refinery
MBPD
Real Forecast
1,200
AAGR 2011-2016
1,000 AAGR 2007-2011 4.5%
3.7%
Demanda
800
Supply Increase with
Current Projects
600 New Tula
Salamanca Refinery
Tula 400
Minatitlan Salamanca
Minatitlán Reconfiguration Reconfiguration
Current Supply
200
Reconfiguración -
2007 2008 2009 2010 2011 2012 2013 2014 2015 2016 2017
New Processing Capacity
Imports, %
Current Operation 40.0 43.1 40.5 47.1 46.7 46.9 47.7 50.5 52.3 54.2 57.7
With New Projects 40.0 43.1 40.5 47.1 43.4 38.7 40.3 39.5 42 35.3 32.5
Gasoline Supply/Demand Balance in México
Producción
Supply Demanda
Demand
New Tula
Salamanca Refinería
1000 Salina Cruz 181
Tula
Minatitlán: 64
800
600
400
200
0
1995 2000 2005 2011 2015 2016
Objectives
Investment:
Schedule:
3 years
29
ULS Gasoline and Diesel
Production Project
ULSG Production Projects (Investment = 2,100 MMUSD)
BAJA CALIFORNIA
SONORA
CHIHUAHUA
SINALOA Cadereyta
DURANGO NUEVO LEON
TAMAULIPAS
Madero
• 2 GHDT 20 MBPD
• 2 Amine Regeneration Unit
ZACATECAS
Madero
Salamanca NAYARIT
AGUSCALIENTES
COLIMA
EDO. MEX.
Tula
D.F.
TLAXCALA
VERACRUZ
CAMPECHE
Tula
MICHOACAN
PUEBLA
MORELOS
• 1 GHDT 32 MBPD
TABASCO
Minatitlán
• 1 Amine Regeneration Unit GUERRERO OAXACA
CHIAPAS
Salina Cruz
Salina Cruz
• 2 GHDT 25 MBPD 31
• 2 Amine Regeneration Unit
ULSD Production Projects (Investment = 4,550 MMUSD)
Total distillates
131 187
10
(gasoline, jet fuel and diesel)
7
Paraffins and Lube Bases
63
Distillates 87 Gasoline
Production
(MBPD 61
Salamanca Actual
Current Operation Salamanca
RCP
(2008)
(2008) Reconfigurada
(1) % Maya refers to the total processing at the Refinery. Maya % in the energetic train amounts to 35%.
35
Refinery Configuration RCP
To Middle Distillates
Middle Dist. HDT Pool
Cat
Gasoil HDT Naphtha
Vaccum FCC 25 MBPD
57 MBPD Post-
Distillation
Treatment
Coker
H-Oil Gasoil
Middle
Diesel HDS
Vaccum
Distillate
ULSD
Residue Pool
Delayed Coker
44 MBPD Coker Naphtha
Sulfur Recovery To Reformer
HDT Blending
Hydrogen Unit 8.8 MBPD
Coke
36
192 MBPD Crude Oil
65 Isthmus/35 Maya 61 MBPD Diesel
Current Configuration
63 MBPD Gasoline
40 MBPD
FCC Unit
53 MBPD Gasoil
Residuals
New Units:
• Delayed Coker 44,000 BPD
• Coker Naphtha HDT 8,800 BPD
• Gasoil HDT 57,000 BPD
• CCR Naphtha Reformer 11,000 BPD
• Sulfur Recovery 300 TPD
• Hydrogen Production 100 MMPCSD
• Sour Water Treatment 30,000 BPD
Revamps:
• FCC 40,000 a 50,000 BPD
• Lube Train 8,800 BPSD
RCP Configuration
Vaccum Hydrotreated
Residue from
VGO Gasoil
Lube Train (400 ppm S)
CGO
Residue Delayed Coker Gasoil HDT FCC
Slops
To H2 Ring
Natural Gas H2
Plantas Incluidas
Other Projects in the Salamanca
Reconfiguration
■ The RCP will be carried out simultaneously to other projects to get sinergy in terms of
economics and opeartional logistics
Business Case
Conceptual Engineering
Technology Selection
Development of Basic
Engineering and FEED
(FEL II y III) - PMC
Preparation of bases
for bidding
EPC Bidding
EPC Execution
41
Tula New Refinery Project
Tula New Refinery Project
HDSD 1
ATM + VACUMM
250 MBPD DISTILLATION
ALK
96 MBPD
HDS G FCC
B-B
P-P from
COKER 1
from COKERS
75.7 MBPD Cokers
COKER 2
Gasoline Specification
Gasoline Pool Structure, Tula New Refinery
6M
“Clean octane” + Oxygen +
RVP
Ethanel
48M
22M “Clean octane” vs. RVP
Isomerization
Premium
BPSD
Business Case
Conceptual Engineering
Technology Selection
Development of Basic
Engineering and FEED
(FEL II y III) - PMC
Preparation of bases
for bidding
EPC Bidding
EPC Execution
Economical Issues
Conclusions
…Thank you