© 2010 Aspen Technology, Inc. All rights reserved
April 28, 2011
Optimizing Flare System Performance at the Valero Sunray Refinery
Presented by: James Holoboff Process Ecology
Outline
• Background
• Application 1: Options for reducing backpressure • Application 2: Addition of a Flare Gas Recovery Unit • Demo
• Improving the Workflow: Automatic transfer of
data to Aspen Flare System Analyzer (Flarenet)
Who are we?
• Valero
– Fortune 500 company based in San Antonio
– North America’s largest independent petroleum refiner and marketer
– 14 refineries and 10 ethanol plants
• Process Ecology
– Engineering Consulting Company – Founded 2003 in Calgary, Alberta
– Team’s experience in engineering consulting, engineering
Benefits
• Flarenet can be used to quickly identify the best alternatives for reducing backpressure
• Flarenet can be used to review the impact of adding an FGRU
• FGRU represents a significant opportunity to recover fuel gas
• Automatic Transfer of data to Flarenet is possible and saves time
Background
• Process Ecology developed a Flarenet model for Valero as part of a refinery flare system upgrade
– Main objectives: verify seal drum levels,
determine crossover sizes/locations, review various scenarios
• Initially a “high-level” model was developed, and later expanded as needed
Applications of Flarenet
• Application 1: Options for reducing backpressure
• Application 2: Addition of a Flare Gas Recovery Unit
• Improving the Workflow: Automatic transfer of data to Aspen Flare System Analyzer
Application 1: Options for addressing
excessive backpressure
• Options for addressing excessive backpressure • Simulation
Using Flarenet to review options for
reducing backpressure (1)
• PSV Selection: check backpressure; impact of valve type on backpressure
For conventional valve, backpressure should not exceed 10% of set pressure; consider balanced or pilot valves if backpressure excessive
Using Flarenet to review options for
reducing backpressure (2)
• Jumpovers: impact of jumpovers to relieve local backpressure High backpressureUsing Flarenet to review options for
Reducing backpressure (2)
• Jumpovers: impact of jumpovers to relieve local backpressure New jumpover Backpressurereduced Backpressurereduced Increase in backpressureUsing Flarenet to review options for
Reducing backpressure (3)
• Line size changes: for existing flare systems, this might mean replacing pipes, or running a parallel flare line
• Moving loads: There may be options for moving a load to a different part of the flare system; if there are
Simulation –
Scenario Management
• Managing scenarios which incorporate
different proposals for reducing backpressure
• Flarenet Scenarios can accommodate PSV changes (flow, conditions) but not differences in line size / structure / ignored pipes / etc.
• Two options:
1. Keep separate cases, or
2. Track changes in a spreadsheet (possibly for import).
Case Header Size Jumpover?
Option 1 8" No Option 2 8" Yes Option 3 10" No
Simulation –
Improving convergence / speed • Tips for improving convergence and speed– After significant changes, clear estimates (in
Scenario Editor)
– Make modifications to flare model in steps
– Check for convergence to reasonable
tolerances (not always obvious)
– Check tolerances
Results
• How simulation helped quantify the impact of
different scenarios and determine the best course of action
Back Pressure (psig)
PSV Mass Rate (lb/hr) Set Pres. (psig) MABP (psig)
Base Case Case #1 Case #2 Case #3 Case #4
PSV #1 8,000 250 25 57.1 106.0 61.6 50.3 70.9 PSV #2 8,000 250 25 57.1 106.0 61.6 50.3 70.9 PSV #3 8,000 250 25 56.3 105.6 60.9 49.5 70.3 PSV #4 19,783 150 105 78.7 119.5 82.6 74.8 87.6 PSV #5 19,783 150 105 80.3 120.6 84.2 76.4 89.1 PSV #6 130,965 235 117.5 82.3 121.1 85.5 78.2 78.6 PSV #7 20,860 270 135 76.5 117.4 79.9 71.1 72.4 PSV #8 759 365 182.5 75.6 116.8 79.0 70.1 71.4 PSV #9 7,220 265 132.5 77.4 117.9 80.7 72.0 73.3 PSV #10 132,165 180 90 44.0 55.9 55.9 44.4 55.9 PSV #11 39,158 280 140 44.1 56.0 56.0 44.5 56.0 • Change PSV #1 / PSV #2 / PSV #3 to balanced PSV
Application 2: Addition of a Flare Gas
Recovery Unit
• What is an FGRU? • Benefits of an FGRU • Simulation • ResultsWhat is an FGRU?
• FGRU = Flare Gas Recovery Unit
• Usually a liquid ring / vane compressor
– Liquid used to mitigate explosivity risk
• Recovers gas in flare system due to ‘everyday’ releases (purges, vents, leaking valves, tank vents, etc.)
• Vacuum on flare system can affect seals – design must take this into account.
What are the benefits of an FGRU?
• Economic savings
– Benefit from recovering and reprocessing blanket
gas, other light gases
• Less flaring – less wear on flare equipment, less visible flare to surrounding neighbors • Regulatory
– Many jurisdictions requiring FGRUs to reduce
How do you simulate an FGRU? (1)
• Compressors
– Flarenet will not model compressor directly, use a
‘flare tip’ with a defined inlet pressure (e.g. Compressor suction pressure)
• Seal Drums
– “Flow Bleed” with fixed pressure drop used during
How do you simulate an FGRU? (2)
• What to do in model with flares during routine venting
– Not a typical ‘flare scenario’
– Manually Turn off flares, run model with FGRU On
– Check Seal Drums to see if DP of seal exceeded,
How do you simulate an FGRU? (3)
• What scenarios do we need to run?
– Challenge to ensure ‘normal venting’ and all major
flare scenarios are defined.
– Especially challenging when multiple flares are
Results
• Simulation helped design of compressor
suction piping & determine seal drum levels
– Identified excessive losses in compressor suction
piping, suggested alternative sizing.
– Identified where the biggest savings in pressure
loss were to be had, allowing only essential piping to be upsized.
– Identified losses in piping so that seal drum levels
could be adjusted and minimum DP in seals maintained during normal operation.
Improving the Workflow
• Benefits of the Valero “Connector Application” • Using Connector Application
Plant Pressure Management / Documentation Tool
Aspen Flare System Analyzer
Transfer PSV / Scenario Data
Benefits of the Connector Application
• Enables automatic transfer of data from plant pressure protection management /
documentation tool (Siemens PPM)
– PPM used for refinery flare system / PSV
management
• As information changes in PPM, the Flarenet model can be automatically updated
Using the Connector Application
1. Select PPM File Location and Flarenet File
2. Mapping: PPM Source / Scenario to Flarenet Source / Scenario 3. Compare Flarenet to PPM Data
4. Export Flarenet input file
5. Save Connector Application File
1 2
3
4
Using the Connector Application
• Comparing Flarenet to PPM Values
Using the Connector Application
Quantifying the Benefits
• Flarenet can be used to quickly identify the best alternatives for reducing backpressure
– Appropriate decisions can be made quicker using a flare analysis tool – hundreds of hours over the course of
supporting flare operations
• Flarenet can be used to review the impact of adding an FGRU
– Associated decisions such as inlet pipe sizing and seal drum heights can be made; e.g., allowing only essential piping to be upsized
– Cost savings associated with correct pipe sizing could be in range of $tens of thousands
Quantifying the Benefits
• FGRU represents a significant opportunity to recover fuel gas
Source: John Zink Based on $2/MMBTU
Quantifying the Benefits
• Automatic Transfer of data to Flarenet is possible
– “Connector Application” provides significant
time/cost savings; reduced manual data entry and associated entry errors
• Manually transferring data (Flow, MW, conditions) for 50 PSVs would take several hours
• With Connector Application this would take a few minutes with no errors in data transfer
• For a few scenarios it would easily represent significant time savings (10-30 hours)
Concluding Remarks
• Flarenet is an effective application for analyzing flare system modifications
• Flarenet can be successfully used to review the impact of flare gas recovery unit
• Workflow can be improved by automating the transfer of data to Flarenet
Thank you!
• Valero
• Alan Swiedom and Laura Chutny • AspenTech
© 2010 Aspen Technology, Inc. All rights reserved | 34
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Flare Network Design and Rating Training
Flare Network Design and Rating: (EHY2511)
May 2, 2011 – Houston, TX May 13, 2011 – Pune, India June 21, 2011 – Virtual – Americas July 14, 2011 – Melbourne, Australia
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• Perform equipment sizing, rating, and debottlenecking of flare systems
using the reporting utilities of Aspen Flare System Analyzer
• Solve convergent, divergent and looped networks
• Reduce calculation time and improve accuracy using tips and best
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• Take advantage of the two-phase modeling capabilities of Aspen Flare
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Contact Information
James Holoboff Process Ecology
Email: [email protected]
Glenn Dissinger
AspenTech (Aspen HYSYS family product manager) Email: [email protected]
Ken Dooley
AspenTech (industry marketing) Email: [email protected]