uop oleflex™ pdh technology - globuc · 2020. 7. 17. · uop oleflex pdh technology evolution e...
TRANSCRIPT
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UOP OLEFLEX™ PDH TECHNOLOGY: INNOVATION, PERFORMANCE AND RELIABILITY
JEFFREY WERY TECHNOLOGY MANAGER – OLEFINS
July 10, 2020
©2020 by Honeywell International Inc. All rights reserved.
GBC⏐ Moscow, Russia
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Agenda
❑ Market Need for On-Purpose Propylene ❑ UOP Oleflex™ Technology Evolution ❑ Latest Catalyst & Process Innovations ❑ Why Customers Choose Oleflex ❑ Honeywell Forge Process Advisor (Connected Solution) ❑ Market Success of Oleflex
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©2020 by Honeywell International Inc. All rights reserved.
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Propylene Market: CIS Supply/Demand Growth
Historic Demand Growth Returns in 2021 ; Lost Year due to COVID©2020 by Honeywell International Inc. All rights reserved.
• Healthy growth rate over next 10 years (8.0% CAGR) • Majority of demand comes from polypropylene (75%) • Steam crackers main source for propylene (60%) • 2.7 MMTA of new capacity forecasted by 2029 • Majority of new capacity will come from PDH (56%) • Region will remain net exporter of propylene
0
50
100
150
200
250
300
350
400
14 15 16 17 18 19 20 21 22 23 24 29Imports Exports
CIS & Baltic States: PG/CG Propylene Trade
Source: IHS Markit © 2020 IHS Markit
Forecast
Thou
sand
Met
ric T
ons
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Propylene Supply & Demand - Global
• “Propylene Gap” is growing - Steam Crackers shifting to lighter feedstocks,
which produce less propylene - Refiners limited by flat gasoline growth in
some regions, which limits propylene from FCCs
• “On-Purpose Propylene” is filling the gap - Propane Dehydro (PDH) - MTO (from gas & coal) - High Severity FCC - Olefin Cracking - Metathesis
On-Purpose Propylene will supply >30% of global propylene by 2027Data Source: IHS Markit (2018)
©2020 by Honeywell International Inc. All rights reserved.
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UOP Oleflex PDH Technology EvolutionC
CO
P R
educ
tion
from
Bas
e
80 %
82 %
84 %
86 %
88 %
90 %
92 %
94 %
96 %
98 %
100 %
% ROI Improvement from Base
0 9 18 27 36 45
Oleflex 1990 DeH-6 Catalyst 1.25 MT C3/MT C3=
Oleflex 1997 DeH-12 1.21 MT/MT
Oleflex 2004 DeH-14 1.18 MT/MT Energy Reduction
Oleflex 2011 DeH-16 1.16 MT/MT Energy Reduction
Oleflex 2015 1.14 MT/MT Energy Reduction
Oleflex 2020 DeH-26
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Catalyst Innovation to Increase Capacity/Reliability
New DeH-26
Shorter Startup Time
Extended Run Length
Increased Hydraulic Capacity
• Larger diameter pills
• 4 year catalyst life expected
• Custom-designed support using recently enhanced manufacturing techniques & know-how
• Optimized metals content achieve high yields & excellent activity
- Continuing use of Platinum as active metal
• First commercial installation 2020
For 600 kMTA unit, can deliver up to an additional $36M of gross margin
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©2020 by Honeywell International Inc. All rights reserved.
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Process Innovations to Extend Onstream Time
Incorporated into Operating Units and New Designs Since 2018
Achieve 4 Year Run
Length
Significantly Lower Reactor Temperatures
(Reduce carbonaceous
fouling)
New Reactor Internals w/ Even More Open Area (Increase fouling
tolerance)Enhanced Sulfur
Injection (Reduce iron
sulfide fouling)
©2020 by Honeywell International Inc. All rights reserved.
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Enhanced Reactor Internals With More Open Area
Generation 1 Generation 2 Generation 3
Rx
Del
ta P
Ris
e
Time
More Open Area, Greater Fouling Tolerance, Increased Onstream Time
In Use
DeH-26 Catalyst (20% larger diameter)
DeH-16 Catalyst
+50% from Base +70% from Base Open Area:
350 kMTA Unit (Gen 2 vs Gen 1)
©2020 by Honeywell International Inc. All rights reserved.
Commercializing Soon
Base
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Process Innovations to Lower Cash Cost of Production
Lower H2 / HC Ratio in Reactor
(enabling lower Rx
temperatures)
New Cryogenic Separation
System Design
(enabling lower H2/HC
ratio) Lower Propane
Consumption (
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Process Innovations to Reduce Capital Cost
Lower CAPEX Improves Project Economics
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©2020 by Honeywell International Inc. All rights reserved.
• Three (3) Reactor Design for PDH Unit • Removes one Reactor, Fired Heater and associated CCR equipment • Lowers CAPEX by ~5% saving ~$20MM USD (for 600 KMTA) • Reduces plot area & maintenance turnaround scope
• Improved Hot Combined Feed Exchanger (HCFE) • Replaces “Texas Tower” design with Spiral Tube exchanger
• Reduced # of shells lowers CAPEX by $8MM USD (for 600 KMTA)
• Improved efficiency lowers OPEX by $1.1MM/yr fuel (for 600 KMTA at $7/MMBtu)
• Maintains UOP’s Latest Process Innovations • Reduced Fouling via Lower Reactor Temperatures • Increased Fouling Tolerance via More Open Reactor Internals • Improved Yield with Low Propane Consumption
CCR
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Comparison of Oleflex with Competing PDH Technology
Characteristic Competing PDH Technology Oleflex
Reactor Type Fixed Bed Cold Wall
Radial Flow Hot Wall
Relative Catalyst Inventory 20 x Base Base
Catalyst Changeout 30-day shutdown No shutdown required On-the fly changeout
# of Reactors• 3 (300 kMTA) • 5 (600 kMTA) • 8 (750-900 kMTA)
4 (all plant sizes up to 900 kMTA) 3 (reduced CAPEX for under 660 KMTA) Easily scalable
Mode of OperationCyclical
(Swing Bed System)Continuous
(Continuous Catalyst Regeneration)
Reaction Cycle Time Frequent (< 10 min/cycle)
Continuous, Stable Operation
Oleflex: Easily Scalable & Continuous Stable Operation©2020 by Honeywell International Inc. All rights reserved.
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12Benefits of UOP Oleflex vs. Competing Technology
Lower CAPEX• $55M-75M savings
(15-20% lower) • (US Gulf Coast
basis; 600 kMTA unit)
Lower OPEX• $6M/year savings or
$10/MT propylene • (600 kMTA unit)
High Plant Productivity• Up to $10-15M/year additional
gross margin from higher onstream availability
Smaller Environmental Footprint• Significantly lower emissions
(NOx, NH3, CO2, VOC, waste water)
• Lower impact on environment
Fast Execution• Fast-to-Market approach
enables startup as fast as 24-36 months
Oleflex Benefits
Dependable Investment• Safe, proven and reliable
process & catalyst technology
Customer Validation• Extensive global acceptance of technology • UOP awarded 68 of 94 units since 2011 • Multiple repeat customers and switches from
competing technology
C3 Oleflex can deliver up to $20M/year lower Net Cost of Production and an additional $80M of NPV and +3% ROI
©2020 by Honeywell International Inc. All rights reserved.
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Honeywell Forge Process Advisor Connected Plant Solution for Oleflex
What is behind it? • Matches unit configuration • Tuned UOP process models • Technology-specific fault models • Embedded UOP knowledge,
context, and background
What does it do? • Monitoring of unit performance • Identify process constraints • Event detection and mitigation • Knowledge transfer
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Connected Process
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Improve Operation
• Continuously identifying key process constraints • Interacting with the customer to implement improvements • Driving the unit to its ultimate performance
Knowledge Access
• Essential information is delivered quickly • Continuous upgrades as new information becomes available
Reduce Issue Response Time
• Issues are quickly identified and the appropriate action is recommended.
• Fast response ensures stable production and potentially avoids an unplanned shutdown
$5.7M total in gross
margin improvement
Typical ValueGap How
Value of Process Advisor for Oleflex14
Assumptions: 450 KMTA production, $350/MT Feed/Product Spread @ 8000 hr/yr Avoiding a 7 day shutdown, ½% production increase, 3 yr
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UOP Leads in Dehydrogenation
©2020 by Honeywell International Inc. All rights reserved.
UOP awarded 68 out of 94 dehydrogenation projects globally since 2011 Since first commercialized, 15 repeat customers & 9 switches from competing technology
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