MERTC 23 rd 24 th January, 2017 Manama, Kingdom of Bahrain

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Future Challenges and Needs of the Refining Industry MERTC 23 rd 24 th January, 2017 Manama, Kingdom of Bahrain Dr. Dawood Nassif Board Director, BAPCO D. Nassif MRTC, January, 2017

Refiner s Challenges D. Nassif MRTC, January, 2017 1

Key challenges for Refiners Crude and Product pricing Sustain long-term profitability in uncertain market conditions Lower operating costs Change in Product Specifications Agility and flexibility to adapt to the latest technologies Meet environmental regulations and future policy changes Availability of skilled manpower for project implementation and operations D. Nassif MRTC, January, 2017 2

Refinery Competitiveness Refinery Competitiveness is driven by the following parameters: petrochemicals D. Nassif MRTC, January, 2017 3

Factors affecting Refining Margins Asia and the Middle East will continue to lead world demand growth for refined products. Product demand growth in the most developed markets over the medium to long term will be dampened by measures to improve vehicle efficiencies and control of green house gas emissions. Ongoing refining capacity developments are expected to be located in the Middle East and Asia. Investment in new refining capacity has slowed in most regions. Increases in US crude oil production will provide cost-advantaged crude oil supplies. Additional refining capacities in the Middle East and upgrading of Russian refineries will increase pressure on European refineries. Increased production of biofuels will reduce demand for gasoline. D. Nassif MRTC, January, 2017 4

Industry Outlook D. Nassif MRTC, January, 2017 5

Petroleum Product Demand Outlook Total global demand for refined products in 2030 is projected to be 42 percent above 2010 levels Diesel/gas oil demand will grow the most Incremental Global Oil Product Demand, 2010-2030 (million barrels per day) D. Nassif MRTC, January, 2017 6

Diesel/Gas Oil Demand Outlook Global diesel/gas oil demand is forecast to grow 2.2%/year, increasing to over 13 MMBPD by 2030 Asia will have the strongest growth (3.1%/year) Incremental Global Diesel/Gas Oil Product Demand, 2010-2030 (million barrels per day) D. Nassif MRTC, January, 2017 7

Gasoline Demand Outlook Global gasoline demand is forecast to grow at an average rate of 1.3%/year, increasing to over 6 MMBPD by 2030 More ethanol use will dampen increased demand for petroleum-derived gasoline Incremental Global Gasoline Demand, 2010-2030 (million barrels per day) D. Nassif MRTC, January, 2017 8

Fuel Oil Demand Outlook Global residual fuel oil demand is forecast to grow by less than 1 MMBPD or 0.5%/year Essentially flat demand will put continued pressure on fuel oil pricing Incremental Global Fuel Oil Product Demand, 2010-2030 (million barrels per day) D. Nassif MRTC, January, 2017 9

Middle East Trends D. Nassif MRTC, January, 2017 10

Middle East Demand Growth Middle East refined product demand growth is above global averages; will be up 4+ MMBPD (2.8% per year) Major refined product production is expected to increase nearly 5 MMBPD, reflecting the surge in project development that is taking place in the region Middle East will continue to be a net exporter of diesel and other middle distillates, but is expected to shift from being a net importer of gasoline to a net exporter. However, the region s future gasoline trade position is heavily dependent upon developments in Iran, and thus is subject to considerable uncertainty. The region is proceeding with very large scale investment in both refining and petrochemicals driven by ambitions to diversify economies. D. Nassif MRTC, January, 2017 11

Future GCC Trends Factors that can affect future growth of refining industry in the GCC region: Market share of exports of refined products Internal demand for fuels Other competing national initiatives D. Nassif MRTC, January, 2017 12

Bahrain National Outlook D. Nassif MRTC, January, 2017 13

Stakeholder s Vision To balance economic growth objectives, domestic industrialization and crude oil sales. Sustained profitability of one of Bahrain s leading contributors to the GDP, in light of rapidly evolving global business scenario. Enhancement of Bahrain s image in the world as a business friendly nation that is developing at a healthy rate. Technical training of Bahrainis and their employment in local industries Meet and exceed the requirements of all environmental regulations D. Nassif MRTC, January, 2017 14

Bapco Modernization Program (BMP) D. Nassif MRTC, January, 2017 15

An Introduction to Bapco The Bahrain Petroleum Company (Bapco) is wholly owned by the Government of Bahrain. The Bapco Refinery was established in 1936 and over the years, it has seen numerous expansions and modifications in response to changing market requirements and product needs. The Bapco Refinery the first in the Gulf refines over 260,000 barrels of crude every day. The Bapco Refinery produces a full range of products, with the most valuable products being middle distillates which constitute about 58% of the refinery production. We have now embarked on the Bapco Modernization Program (BMP). D. Nassif MRTC, January, 2017 16

Bapco s History and Evolution BAPCO established by Standard Oil Company of California The Bahrain Refinery is inaugurated with a capacity of 10,000 barrels per day Bahrain Refinery expansion program completed with 250,000 b-day capacity Start-up of Ultra Low Sulphur Diesel Complex 75 years after first oil discovery Inauguration of Waste Water Treatment Plant at a cost of USD120 million 1929 1932 1936 1945 1968 2004 2007 2011 2013 2014 First oil discovery in the Arabian Gulf: Well #1 in Bahrain Original A-B pipeline laid between Bahrain and Saudi Arabia. Commenced construction Low Sulphur Diesel Production Project (USD1.1 billion) Inauguration of joint venture Lube Base Oil Plant (USD430 million) Inauguration of Bapco Lubricants 1930s; 1 st oil well 1940s 1960s Today D. Nassif MRTC, January, 2017 17

BMP Objectives Driven by the aspiration to remain competitive and continue its traditional role as a key contributor to the national economy, Bapco launched its ambitious Bapco Modernization Program (BMP) that would place it amongst the most competitive and profitable refineries in the region beyond 2020. BMP s objectives are: Refinery Configuration and Gross Margin A modernized Refinery configuration that allows for higher throughput, improves the product slate and increases gross margin with the objective of remaining competitive under a wide range of prices and market scenarios Energy Efficiency Improve energy efficiency and lower the Energy Intensity Index (EII) of the Refinery by installing new energy-efficient process units Environmental Compliance All new units will function in compliance with applicable local environmental regulations and World Bank guidelines. D. Nassif MRTC, January, 2017 18

BMP Technology Selection Process A Preliminary Assessment carried out for BMP to meet project objectives and modernize Bapco established that the most effective way of improving gross margin was to concentrate on middle distillates production at an increased refinery capacity with resid conversion units to reduce or eliminate fuel oil. Selection of the most appropriate residue upgrading technology was one of Bapco s biggest challenges. Bapco evaluated multiple combinations of residue conversion technologies with the following intent: maximize the most valuable product (diesel) while retaining the capability to address niche product demands for the foreseeable horizon be commercially proven, environmentally compliant, reliable and operationally flexible have enough complexity so that the Refinery remains profitable when margins remain depressed for prolonged periods. Based on current trends only such refineries will survive in the future. D. Nassif MRTC, January, 2017 19

Resid Upgrade Technologies Bapco evaluated the following residue upgrading technologies and technology combinations for a range of refinery capacities: - Ebullated Bed Residue Hydrocracking Unit (RHCU) - Delayed Coking (DC) - Fixed Bed Residue Desulphurization (RDS) - Solvent Deasphalting (SDA) - Residue Fluidised Catalytic Cracking (RFCC) These technologies cover commercially proven options available for a modern refinery. Their combinations were also evaluated under a broad range of crude slate and multiple sensitivity constraints. The RHCU route offered the highest IRR for the range of crude capacities evaluated. D. Nassif MRTC, January, 2017 20

Post BMP Refinery Existing Refinery Units*: KSA 305 MBPD Arab Light Crude supplied via the new AB Pipeline (capacity up to 350 MBPD) 5 Crude Units 3 Vacuum Units Diesel Hydrodesulphuriser Unifiner/Platformer VGO Hydrocracker FCCU Visbreaker Hydrogen Plants Sulphur Recovery Units Base Lube Oil New Refinery Units: 50-60 MBPD Local Bahrain Crude Production 2 Crude Units 2 Vacuum Units Residue Hydrocracking Unit 2 VGO Hydrocracking Units 2 Diesel Hydrotreating Units Hydrogen Plants Sulphur Recovery Units Saturated Gas Plants D. Nassif MRTC, January, 2017 21

Scope of BMP Crude Unit 225 MBPD Vacuum Unit 100 MBPD Residue Hydrocracking Unit 65 MBPD VGO Hydrocracking Unit 58 MBPD Diesel Hydrotreating Unit 50 MBPD Hydrogen Plants 2 x 125 MMSCFD Sulphur Recovery Units 3 x 250 MTPD Saturated Gas Plants 2 x 30 MMSCFD Offsites, Utilities, Revamps/Upgrades D. Nassif MRTC, January, 2017 sized to match 22

Improved Competitiveness Post BMP, Bapco s size will increase from 267,000 to 360,000 bpd and its complexity will increase from 6.3 to 7.1 BPD D. Nassif MRTC, January, 2017 23

Refinery and Petrochemicals Integration D. Nassif MRTC, January, 2017 24

Aromatics Production Complex (APC) The APC is a 50-50% Joint Venture between nogaholding of Bahrain and PIC of Kuwait. The APC presents an attractive opportunity. The Heavy Naphtha from BMP will be used as APC feedstock to be converted into high-value products such as Para-Xylene and Benzene. APC will produce Hydrogen as a valuable by-product. BMP needs significant amounts of Hydrogen, where about half the requirement will be supplied by the APC. Aromatics production is likely to remain attractive for a long period because the supply tightness is structural. UOP has been selected as the technology licensor for the APC. D. Nassif MRTC, January, 2017 25

Adding Value to Crude D. Nassif MRTC, January, 2017 26

Thank You! D. Nassif MRTC, January, 2017 27