Focus on Slurry Hydrocracking Uniflex Process Upgrade Bottom-of-the-Barrel to Improve Margins Phil Hunt UOP LLC, A Honeywell Company Russia & CIS BBTC 2015 April 22-24, 2015 Moscow A Century of Innovation in the Oil and Gas Industry 2015 UOP LLC. All rights reserved. UOP 7081-1
Agenda 1 2 3 4 5 Market Opportunity, Russian Export Duties, Demand UOP Residue Upgrading Technology Portfolio UOP Uniflex Technology Update Mendeleev Group Deep Processing Project Summary 2 UOP 7081-2
Million barrels Per Day Global Refined Product Demand has Followed a Consistent Trend... 40 40000 35000 30000 25000 20 20000 15000 10000 5000 0 0 1970 Global Oil Product Demand (Fuel Oil and Distillates) Middle Distillates Light Distillates Heavy Fuel Oil 30 year trend 1980 1990 2000 2010 1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 0 Source: BP Statistical Review of World Energy 2013 Global HFO demand equaled each of Light and Middle Distillates in 1970 Distillates have now passed 70% of total demand globally Globally HFO has declined to 10% of total product demand In Asia, the Light Distillate demand is driven by Petrochem Feedstock end-uses 3...with Distillate demand increasing and Fuel Oil demand declining UOP 7081-3
There are 3 Parts to the European Fuel Oil Market Bunkers 80 40 80 (Units presented are MTPA) Source: EIA Statistical Data 65 HFO 40 1 2 3 HFO Exports Demand Production Imports 1 2 3 European Fuel Oil demand is split between Marine Bunkers and HFO Production currently aligns with demand However, Europe also imports and then exports 65 million MTPA 3 65 Europe is very long in HFO (particularly HSFO) 4 UOP 7081-4
Why do we also need to understand developments in Russia and their impact on European HFO? Russia has... Third highest installed refining capacity (after U.S. and China) The largest production of Vacuum Residue that is not upgraded, the majority of which is exported to Europe Most of Russia s Fuel oil exports go to Europe Russia recently introduced... New export duties on crude oil and products (so-named 60-66 ) These provide significant incentive to upgrade HFO into Distillate products Russian refiners plan to invest $50 billion to minimize HFO exports 5 UOP 7081-5
Marine Bunker Fuels: EU and IMO Developments Sulphur content allowable in bunker fuel (pc by weight) 5.0 4.5 4.0 3.5 3.0 2.5 2.0 1.5 1.0 0.5 0.0 Jan 05 Mar 06 Global Emission Control Areas May 07 Jul 08 Sep 09 Nov 10 Jan 12 Mar 13 May 14 Jul 15 Sep 16 Nov 17 IMO reduction timing subject to study re availability to be undertaken in 2018 Jan 19 Mar 20 May 21 Jul 22 Sep 23 Nov 24 IMO (MARPOL) Regulations ECAs: Sulphur reduces from 1.0% to 0.1 % (January 2015) EU: Sulphur reduces from 3.5% to 0.5% (January 2020) Rest of the World: Sulphur reduces from 3.5% to 0.5% (January 2020/2025) 6 UOP 7081-6
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 Feedstock characterisation is a key parameter in residue processing with composition, properties and molecular structure all important factors 7 UOP 7081-7
UOP Solutions for Residue Conversion (Low to Moderate Conversion Options) UOP RCD Unionfining Process UOP/FWUSA Visbreaking FWUSA SYDEC Delayed Coking Process Limited conversion and feed flexibilty LS fuel oil production or RFCC feed prep Emerging role again Up to 30% conversion Achieves reduction in cutter stock for fuel Can be a partial fix, not a full solution Fuel oil outlet needed Higher conversion - up to 75% Require further upgrading to meet final product specs Need an outlet for the pet coke 8 UOP 7081-8
UOP / FWUSA Solvent Deasphalting... De-Asphalted Oil (DAO) feed to: FCC HCU Vacuum Residue (VR) SDA Not a conversion process, but a solvent / gravity separation process Separation also driven by the molecular type - paraffins vs aromatics 9 SDA Pitch feed to: Bitumen Boiler / Power DCU Uniflex Unit DAO yield ( lift ) is typically 40-60+%, limited by DAO quality and at high lifts by pitch quality UOP 7081-9
The UOP Uniflex Technology Offering is... Once through Catalyst Products require further upgrading Offered either as a stand-alone-unit or with integrated DHT Vacuum Residue Feed 100 UNIFLEX UNIT (Wt-%) 15 50-55 H 2 S, NH 3 Gas, LPG Naphtha Diesel HDT 90-95% Conversion Maximum Diesel Minimum VGO Catalyst H 2 10-15 VGO Pitch MHC & FCC or HCU 10 UOP 7081-10
Uniflex Process Thermal Cracking of Asphaltenes The process benefits from combination of: 1. Thermal cracking to shorter chain lengths 2. Inhibiting formation of coke through: Hydrogenation of free radicals from thermal cracking Catalyst physically hinders mesophase coalescence Archipelago Model of Asphaltenes, Carbon # = 313, MW = 4705 Source: M. Gray, Univ of Alberta 11 UOP 7081-11
Uniflex Process Reactor Achieves High Conversion Products and Catalyst Optimal design for high conversion Upflow Near Isothermal Efficient utilization of reactor volume Effective Asphaltene management Inhibit formation of coke pre-cursors by hydrogen pressure, optimum temperature and catalyst 12 Feed, H 2 and Catalyst Simple Commercially proven Reactor design for highly effective performance UOP 7081-12
Catalyst (Additive) & Pitch Catalyst (Additive) UOP global supply Multiple manufacturing locations Simple logistics and storage Cement: Often the most attractive outlet option Boiler/Power: Conventional power plants CFB or Rotary Kiln Furnace Gasification Pitch Solidification: Proven technology (Pellets or Big Bags) Facilitates transportation and storage 13 UOP 7081-13
Hydrogen to Carbon Atomic Ratio Uniflex Process Attributes Summary 3 Converting VR into Diesel Needs 2 DIESEL HYDROGENATION Thermal Cracking and Hydrogenation Uniflex Complex Achieves this 1 CRUDE OIL THERMAL CRACKING VAC RESID In a single slurry bed reactor With Post treatment to meet finished product specifications H 2 addition maximises margin 0 20 40 60 14 Average Carbon Number (Atoms per Molecule) UOP 7081-14
UOP Uniflex Process - Licensed Units Update Name Location Capacity, MMTA Start-up Petro-Canada, Montreal Canada 0.3 1985 NRL, Pakistan Pakistan 0.6 2017 Undisclosed China 0.9 2016 Mendeleev Group Russia 0.4 2017 Undisclosed China 0.8 2017 Undisclosed China 0.9 2017 Undisclosed China 0.8 2017 15 UOP 7081-15
OGT Background Oil Gas Trade (OGT) was established in 2002 Key Business is fuels (jet, diesel, gasoline) and lubricants supply Acquired Yaroslavl Mendeleev Refinery in 2012 New Mendeleev Group Project / Complex Construction of a new 3 MMTA Deep Processing Complex (DPC) Robust economics with Russian export duty regime Zero residue production (via Uniflex & Unicracking) Maximum diesel production Captive Power, Steam & H 2 production 16 100+ year old existing refinery, open to new innovation, planning new Deep Processing Complex UOP 7081-16
It is Essential to assess a Major Project s Rate-of-Return Relative to Risk The early years of a Project s performance are always the most visible Lifetime performance covers a 20+ year period RISK RoR Window of Opportunity Consequences of Pushing the Risk Envelope too Far Reliability Availability Throughput Timeline 17 It is important to evaluate and mitigate any major project risks technical, operational or other otherwise forecast financial returns can be undermined through under-performance UOP 7081-17
Million barrels Per Day Global Fuel Oil is now Entering the Final Stages of Decline, Trending to Zero... 40 40000 Global Fuel Oil Demand 35000 VGO VR 30000 25000 20 20000-3 MBPD 15000-2 MBPD -1.5 MBPD 10000 <10% of Total Demand 5000 18 0 0 1980 1990 2000 2010 0 1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 Source: BP Statistical Review of World Energy 2012 It is realistic to assume further reduction via further switching to natural gas and tighter IMO MARPOL regulations for Bunker Fuels UOP 7081-18
Price spreads and project economics are the main driver of any major residue upgrading project: The Diesel minus HSFO Price Spread is the Key Economic Driver $450/t $350/t EXCELLENT $250/t GOOD MARGINAL Europe Pre 2012 Europe 2013/15 Russia 2014/15 19 Russian pricing offers attractive economic returns UOP 7081-19
Ongoing Innovation in Vacuum Residue Conversion Product - Feed Uplift, $/MT 250 Slurry Hydrocracking Conv 95% 200 150 Ebullated Bed Conv 70% 100 Delayed Coking Conv 70% 20 50 today s pricing Dubbs Conv 25% Visbreaking Conv 15% 0 1900 1920 1940 1960 1980 2000 2020 Year Demand for transportation fuels vs. fuel oil has driven a seven times increase in the gasoline + diesel yield enabling alignment of production with demand UOP 7081-20
Q&A 21 UOP 7081-21