UOP Technologies for Distillate Production
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1 Erik Svensson Hydroprocessing and Heavy Oil Technology Manager May 15, 2017 May 17, 2017 UOP Technologies for Distillate Production Hydrocracking Innovations 2017 Honeywell Oil & Gas Technologies Symposium Cairo, Egypt Alexandria, Egypt
2 Licensed Capacity, BPSD 64 Years in Hydroprocessing Innovations Unionfining Units Unicracking Units 2011 ExxonMobil Lubes & Fuels Alliance Uniflow TM Reactor Internals 4th Generation UOP Hydroprocessing Experience Award Year st Unionfining TM Unit st Unicracking TM Unit 1990s 2006 HPNA Management 2008 E2S Process 2016 Unity TM Hydroprocessing Catalysts UOP 7432D Unionfining Units & 220+ Unicracking Units Licensed
3 Customized Solutions to Meet Customer Objectives Hydrocracking Technology Portfolio Feedstock Unicracking Reactor Section Unicracking Fractionation Section Products 2 Once Through Naphtha Distillate LCO Dual Stripper/Dual Frac Kero/ Jet Fuel VGO Single Stage Recycle Diesel Fuel CGO DAO Two Stage Recycle HPNA Management Lubes EMCL MSDW TM & MAXSAT TM Technology
4 3 Heavy Oil Processing UOP Uniflex Process Portfolio of Multiple Solutions Distillate Dewaxing and Lube Base Oil Production Crystaphase CatTrap Honeywell Process Control Solutions UOP 7432D-3
5 4 Operational Needs Maintaining Throughput End of Run Maintaining Yields Maintaining Product Qualities Improved Profitability and Flexibility Next Cycle Reactor Performance Opportunity Feedstocks Product Slate Flexibility Enhanced Product Qualities Improved Product Yield Long Term Increased Throughput UCO Utilisation High Conversion Improved Energy Efficiency Greater Product Recovery UOP 7432D-4
6 Next Cycle Opportunities 5 Improved Product Yield Increased Cycle Increased Conversion Catalyst Selection - Increased Yields - Improved Product Qualities Increased Conversion - HPNA Management Improved Reactor Performance - Reactor Replacements Opportunities for improved operation - Uniflow Reactor Internals Reduced quench zone height Shorter installation time Easier maintenance Improved Distribution UOP 7432D-4
7 Improved Distribution with UOP Uniflow Reactor Internals 6 New design offering a step change in performance & speed of installation First sale in 2013 Sold into 20 units (new and revamp) with 10 operating successfully Example: Installed in 5-bed HC reactor in Nov, Unit operating at 32% higher feed rate compared to previous cycle. Hydrocracking Bed Bed 1 Bed 2 Bed 3 Bed 4 Bed 5 Customer Feedback: Radial Spread (ºF) New Cycle Top: 1 Bottom: 1 Top: 4 Bottom: 3 Top: 4 Bottom: 2 Top: 4 Bottom: 3 Top: 4 Bottom: 4 Radial Spread (ºF) Previous Cycle Top: 3 Bottom: 18 Top: 2 Bottom: 6 Top: 5 Bottom: 6 Top: 12 Bottom: 36 Top: 11 Bottom: 45 We would never have been able to operate this unit where it is today without these new internals. This is a step change for UOP UOP 7432D-6
8 UOP Uniflow TM Reactor Internals 7 UOP 7432D-7
9 MIDOR Refinery Expansion Project Boosting Refinery Capacity 100,000 to 160,000 BPSD 8 Project Objectives Refinery throughput increased 60% Maximising middle distillate yield Meet future legislation of high quality EuroV specifications Zero fuel oil production Additional Requirements Maximum utilisation of existing refinery units Minimise refinery downtime Limited plot space UOP 7432D-10
10 MIDOR Refinery Expansion Project Boosting Refinery Capacity 100,000 to 160,000 BPSD 9 Crude Oil CDU LPG C D U SRN Kero LPG from other units SGP LPG LPG Merox HC LPG NHT LPG Frac. C 3 /C 4 NS Fuel Gas ISOM Isomerate LPG Euro V Gasoline R95 At Res SRD CDU LPG V D U VGO KHT NAP KHT CCR Reformate Kerosene SRN DHT NAP Crude Oil C D U Kero New DHT HT Diesel Local Diesel SRD HC NAP HC LPG to LPG Frac At Res V D U VGO Pitch DC NAP LCGO Delayed Coker SDA HCGO DAO HC UCO HC Kero HC Diesel New Unit Euro V Diesel Coke Revamp Existing Unit UOP 7432D-9
11 MIDOR Refinery Expansion Project Current Kerosene and Diesel Processing Configuration 10 SR Kerosene Existing Kerosene Merox 11,000 BPSD Jet A1 SR Diesel + LCGO Existing DHT 29,000 BPSD Local Diesel 50 wtppm S Current Configuration Targets local diesel production Kerosene to Jet A1 pool only No ability to achieve EuroV diesel specifications UOP 7432D-12
12 MIDOR Refinery Expansion Project Maximising Euro V Diesel Production 11 SR Kerosene Existing Kerosene Merox 11,000 BPSD Jet A1 SR Kerosene KHT (Revamped DHT) 18,000 BPSD Local Diesel 50 wtppm S SR Diesel + LCGO New DHT 48,000 BPSD Euro V Diesel 10 wtppm S UOP 7432D-13 Ultimate flexibility between Jet A1 and EuroV Diesel production. Minimum shutdown and plot space with optimised investment
13 Make-up Gas Unicracking Unit Existing Configuration 12 Naphtha 33,000 BPSD VGO+HCGO Separation Fractionation Kerosene Diesel UCO 17,000 BPSD UOP 7432D-14
14 Make-up Gas Unicracking Unit New Configuration 13 New RG Scrubber Naphtha 50,000 BPSD VGO+HCGO+DAO Separation Fractionation Kerosene Diesel Uniflow Reactor Internals MUG 35,000 BPSD UCO Common H 2 Recovery Naphtha Separation Fractionation Kerosene Diesel HPNA Management UCO UOP 7432D-113
15 MIDOR Refinery Expansion Project Boosting Refinery Capacity 100,000 to 160,000 BPSD 14 Investment cost of $1.8 billion EPC Phase expected to commence 4 th quarter 2017 Internal rate of return 30% confirming the economic importance of the expansion. Product % Increase LPG 84% High Octane Gasoline 52% Jet Fuel 180% Diesel 33% Total Distillate 75% UOP 7432D-16
16 15 Solutions for Improved Hydrocracking Performance Improved Profitability and Flexibility Industry-leading hydrocracking technology for optimizing the production of high quality fuels Multiple solutions for next cycle and long term opportunities strategies: - Hydrocracking innovations - Bottom of the barrel upgrading - Alliances - Honeywell process solutions Flexible offerings to meet refiners processing and financial objectives Focus on innovation to improve hydroprocessing performance and reduce capital and operating costs UOP can evaluate the product slate, capital expense and operating expense of the overall complex to provide the highest value solution to the customer Combining cutting-edge design and 65 years of experience UOP 7432D-17 to deliver maximum value
17 UOP 7432D-16 16
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