Maximizing Refinery Margins by Petrochemical Integration

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Topic Maximizing Refinery Margins by Petrochemical Integration Presented by : Rajeev Singh

Global Demand for Refined Products 29% 29% 29% 29% 30% 30% 33% 10% 10% 10% 9% 8% 8% 7% 7% 7% 7% 7% 7% 7% 22% 22% 22% 23% 24% 25% 7% 7% 7% 7% 6% 6% 25% 25% 25% 25% 25% 24% 39% 4% 17% Reduced Gasoline & Naphtha demand 2012 2013 2014 2015 2020 2025 Incremental 2012-2025 2016-2025 Gasoline Naphtha Diesel Other Middle Distillate Heavy Fuel Oil Other Source: Hart Energy Research & Consulting

Demand in,000 BPD 2,000 Regional Gasoline Growth Refinery Ethanol 1,500 1,000 500 0 North America Latin America Europe Russia/CIS Asia Pacific Middle East Africa -500-1,000-1,500 - Regional Imbalance in Gasoline Production and Demand - Increased percentage of renewables (EthOH) in Gasoline pool displaces some refined gasoline Export Naphtha or Upgrade? Source: Hart Energy Research & Consulting

MM BPD Tightening Fuel Specifications 30.00 25.00 Global Gasoline Demand (by S Spec) 20.00 15.00 10.00 5.00 Tighter Sulfur Specs in Fuel - Limits naphtha blending into gasoline pool - Desulfurization loss of Olefins & Octane value costly, CAPEX and OPEX Upgrade Instead to Petrochemicals! 0.00 2012 2015 2020 2025 < 10 ppm 11-50 ppm 51-500 ppm > 500 ppm Source: Hart Energy Research & Consulting

Refinery Trends: India Implementation of BS IV in India From April 2017. Gasoline Specification gets stringent to meet BS IV Standards. In rural areas, a shift in Gas for cooking and electricity for lighting has resulted in decrease in Kerosene Demand. There are 23 refineries spread across in India with refining Capacity of 230 MTPA. Surplus Naphtha & Kerosene?

Petrochemicals Outlook WORLD LIGHT OLEFINS DEMAND WORLD OLEFINS DEMAND BY REGION Source: Hart Energy Research & Consulting

Benefits of Refinery Petrochemical Integration > Assured Refinery product uptake > Secure Petrochemical Feedstock availability > Significant savings in investment Shared utilities, infrastructure, logistics > Savings in operating costs Energy integration, Shared Resources > FeedStock & Product Flexibility to Meet market Demand > Improved Gross Refinery Margin (GRM)

KBR Olefins Technology Portfolio What Feeds Features SCORE (Steam Cracking) Off Gas Recovery K-COT TM (Catalytic Olefins) Ethane through Gas Oil Low value refinery Off gases Residence time ~0.08 1.0 sec Low CAPEX Superior Performance Offered via Agreement with ExxonMobil Recovers Most of Ethylene & Propylene Recovers Paraffins (Ethane & Propane ) in recycle Stream Low Capital Cost & Low Energy Consumption Olefinic C4-C10 P/E ratio ~ 2/1 Gasoline by-product >50% aromatics Recycle C4-C6 NA to extinction without additional treating Paraffinic naphtha, light distillates P/E ratio ~ 1/1 Recycle C4s/C5s without additional treating Non-traditional High olefin yields from methanol, ethanol and other oxygenates and MTO/MTP and FT by-products

SCORE TM What Feeds Features SCORE (Steam Cracking) Off Gas Recovery K-COT TM (Catalytic Olefins) Ethane through Gas Oil Low value refinery Off gases Residence time ~0.08 1.0 sec Low CAPEX Superior Performance Offered via Agreement with ExxonMobil Recovers Most of Ethylene & Propylene Recovers Paraffins (Ethane & Propane ) in recycle Stream Low Capital Cost & Low Energy Consumption Olefinic C4-C10 P/E ratio ~ 2/1 Gasoline by-product >50% aromatics Recycle C4-C6 NA to extinction without additional treating Paraffinic naphtha, light distillates P/E ratio ~ 1/1 Recycle C4s/C5s without additional treating Non-traditional High olefin yields from methanol, ethanol and other oxygenates and MTO/MTP and FT by-products

Introduction to SCORE TM SCORE TM, is the traditional steam cracker technology offered in collaboration with ExxonMobil that combines Selective Cracking furnace technology with an Optimum REcovery section. Selective Cracking Optimum REcovery

SCORE TM Furnace Portfolio One pass Two pass Four pass Coil Type Residence Time (sec) 0.1 0.2 0.4 SCORE SC-1 SC-2 SC-4 Competitors No Yes Yes SC-2 SC-4 Single Pass Straight Tube (~ 0.08-0.12 sec) Two-Pass (~ 0.18-0.25 sec) Serpentine-Type (~ 0.35-1.0 sec) Broadest range of residence times in the Industry Highest Ethylene Yield In Industry

SCORE TM Furnace Flexibility Multi-Feed (Hybrid) Cracking Large Capacity Single Cabin Firebox SCORE TM Furnaces 8 individually flow controlled passes Number of Feeds only limited by inlet piping arrangement Each Feed can be cracked at optimum conditions: - Temperature - S:HC Ratio Furnace 1 2 3 4 5 6 7 8 Flexibility of 8 Mini Furnaces within a Single Firebox

Petrochemical Feedstock Flexibility Traditional Feedstock LPG Naphtha Propane Butane Straight Run Paraffinic Flexibility to Crack range of feed Refinery Non-Traditional Feedstock Light Distillate Heavy Distillate Kerosene Gas Oil Recent Trend in Feedstock Off Gas From FCC & DCU Ethane & Propane Ethylene & Propylene SCORE

SCORE TM Reference Facility Gas Oil Naphtha #1 #2 #3 #4 #5 Configuration Four (4) Hydrocarbon Furnace Feeds Furnaces 1 3: 50/50 Flexibility Furnaces 4 5: Full Flexiblity Total No. Cracking Cells: - (3 x 2) + (2 x 8) = 22 Advantages E/P Recycle LPG No Dedicated Recycle Gas Furnace No Co-Cracking: - Feeds cracked at optimum conditions High Flexibility Low TIC Flexibility allows Maximum Profitability

Off Gas Recovery Unit Technology What Feeds Features SCORE (Steam Cracking) Off Gas Recovery K-COT TM (Catalytic Olefins) Ethane through Gas Oil Low value refinery Off gases Residence time ~0.08 1.0 sec Low CAPEX Superior Performance Offered via Agreement with ExxonMobil Recovers Most of Ethylene & Propylene Recovers Paraffins (Ethane & Propane ) in recycle Stream Low Capital Cost & Low Energy Consumption Olefinic C4-C10 P/E ratio ~ 2/1 Gasoline by-product >50% aromatics Recycle C4-C6 NA to extinction without additional treating Paraffinic naphtha, light distillates P/E ratio ~ 1/1 Recycle C4s/C5s without additional treating Non-traditional High olefin yields from methanol, ethanol and other oxygenates and MTO/MTP and FT by-products

Off Gas Recovery Unit Introduction REFINERY DCU OFFGAS FCC OFFGAS OffGas Stream Rich in High Value Olefins Refinery Off Gas- Rich in Olefins, C2 & C3 saturates, normally used as fuel gas. KBR Provides solution to recover high value olefins, C2 & C3 saturates and fuel gas products with - Off Gas Recovery Technology.

Off Gas Recovery Unit Overview STANDALONE PROCESS BLOCK INTEGRATED CONTAMINANT REMOVAL CONTAMINANT REMOVAL RECOVERY SECTION PG ETHYLENE, ETHANE, C3 PRODUCT HIGH HEATING VALUE FUEL GAS REFINERY GAS RECTIFIER PRODUCT- FUEL GAS AND C2+ RICH STREAM INTEGRATED WITH STEAM CRACKER) UTILITIES AND ANCILLARIES BLOCK STANDALONE INTEGRATED PROPYLENE REFRIGERANT CW, STEAM, ELECTRICITY (CAN BE INTEGRATED WITH REFINERY) SAME AS STEAM CRACKER (PR & ER REFRIGERATION, CW, STEAM, ELECTRICITY)

KCOT TM What Feeds Features SCORE (Steam Cracking) Off Gas Recovery K-COT TM (Catalytic Olefins) Ethane through Gas Oil Low value refinery Off gases Residence time ~0.08 1.0 sec Low CAPEX Superior Performance Offered via Agreement with ExxonMobil Recovers Most of Ethylene & Propylene Recovers Paraffins (Ethane & Propane ) in recycle Stream Low Capital Cost & Low Energy Consumption Olefinic C4-C10 P/E ratio ~ 2/1 Gasoline by-product >50% aromatics Recycle C4-C6 NA to extinction without additional treating Paraffinic naphtha, light distillates P/E ratio ~ 1/1 Recycle C4s/C5s without additional treating Non-traditional High olefin yields from methanol, ethanol and other oxygenates and MTO/MTP and FT by-products

Introduction to K-COT K-COT is KBR s Catalytic Olefins Cracking Technology (FCC) that processes light Olefinic, Paraffinic or mixed feeds, resulting in high propylene yields with ethylene and aromatic-rich gasoline by-products. Feed Flexibility High Value Products K-COT

Reactor Converter Proven FCC-based technology Tailored catalyst maximizes propylene yield Smooth Startup Simple operation Low maintenance Wide Feed flexibility

Traditional Integration Scheme Off Gases Crude Oil CDU FCC Isom Hydrotreaters Deasphalting Coker Others Gasoline Distillate Jet / Kero Fuel Oil Off Gas Recovery LPG Naphtha Ethane Propane Hot Section Cold Section Ethylene Propylene Butadiene PyGas Ethylene Propylene

Optimized Integration Scheme Off Gases Crude Oil CDU FCC Isom Hydrotreaters Deasphalting Coker Others Gasoline Distillate Jet / Kero Fuel Oil Off Gas Recovery LPG Naphtha Catalytic Olefins Recovery Ethane Propane Ethylene Propylene Hot Section Cold Section Ethylene Propylene Butadiene PyGas

Typical Ultimate Yields from KCOT TM Unit Paraffinic Feed Olefinic Feed 100 100 90 75 80 50 Other Gasoline Propylene Ethylene 70 60 50 40 Others Hvy Gasoline BTX Propylene 25 30 Ethylene 20 0 Steam Cracker Catalytic Olefins 10 0 C4 Raff-1 C5s FCC LN Coker LN

Conclusion Global trend reflects decrease in demand for Gasoline & Naphtha Petrochemicals show incremental Growth across the world. Market volatility & Sustainability demands Integration of Refinery with Petrochemicals KBR Offers technology with unmatched Feed & Product Flexibility to meet market demand. Higher Flexibility Offers Higher Profit Margin for Refineries.