Training - Day 4 Oct 8 2020 Flare Case Studies...6OLGH .. :*65 ZRUNV ZLWKLQ WKH K\GURFDUERQ...
Transcript of Training - Day 4 Oct 8 2020 Flare Case Studies...6OLGH .. :*65 ZRUNV ZLWKLQ WKH K\GURFDUERQ...
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WELCOME TO THE
CALLIDUS COMBUSTION SCHOOL 2O2O
YOU ARE AT THE RIGHT PLACE, PLEASE WAIT A MOMENTAND THE PRESENTATION WILL BEGIN AT THE APPOINTED TIME
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Callidus Technologies – Leader in combustion solutions
Honeywell Internal
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CASE STUDY: THE nViro™ XSR ELEVATED STEAM FLARE KURT KRAUSPRINCIPAL TECHNOLOGIST
Callidus Combustion School
October 6, 2020
Everywhere Virtual
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CALLIDUS FLARE EXTREME STEAM REDUCTION XSR TECHNOLOGY
• Process Steam Control
• Drone Inspection Service
• AMEL Multipoint Ground Flare Testing
• RSR Development
Callidus Heritage in Combustion Technology World Class Test Facility
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CALLIDUS FLARE EXTREME STEAM REDUCTION XSR TECHNOLOGY
4G: First Major Change in Flare Combustion Technology in Decades
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ELEVATED FLARE COMBUSTION TECHNOLOGY EVOLUTION
Additional Steam Used to Inspirate Air to Reduce Smoke
Generation | Pre 19601st Generation | 1960 Generation | 1990’s2nd 3rd
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ELEVATED FLARE COMBUSTION TECHNOLOGY EVOLUTION BRAINSTORMS
6
Concluded 4G Flare has to Be a Revolution Not and Evolution
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100% SMOKELESS GROUND FLARE COMBUSTION TECHNOLOGY
PATENTS APPLIED FORPropylene Under
Pressure> 5 Psig
Propylene After Depressurization
< 1 Psig
Macro Micro
Gas Pressure Provides Mixing Energy For Smokeless Combustion
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Performance
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AirPropaneSteam
Steam, Gas, Jet
Technology
Steam, Air Mixing
Technology
4G
3G
FLARE COMBUSTION PARADIGM SHIFT #1BETTER AIR/STEAM/FUEL MIXING: MICRO STEAM JET LEVEL
8
4G: Steam Used to Transfer Momentum
FlowGeometry
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PerformanceMixing (Mass Fraction of Air)FlowGeometry
FLARE COMBUSTION PARADIGM SHIFT #1BETTER AIR/STEAM/FUEL MIXING: MACRO FLARE ARM LEVEL
9
4G: Macro Level 40% Improvement in Air mixing
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Callidus R&D2016
4G
3G
KK2KK3
KK4
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Slide 10
KK2 Kraus, Kurt, 9/3/2019
KK3 Maintain Micro Mixing on a Macro level.Kraus, Kurt, 9/3/2019
KK4 Peaks of Steam in Sync with Peaks in Fuel, max fuel and minimum air.Kraus, Kurt, 9/3/2019
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FLARE COMBUSTION | PARADIGM SHIFT #1:
5 MPH Gusting 15-25 MPH Wind
Better Air/Steam/Fuel Mixing
At incipient smoke point
in low and high wind
ADDED BENEFIT: No Muffler Needed, No Exposed Steam Jet, No Jet Noise
This flame is All Burning! Really, it is!
No Flame We See the Steam
PlumeWith
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FLARE COMBUSTION | PARADIGM SHIFT #1:
5 MPH Gusting 15-25 MPH Wind
This Flame is Burning! Really, It Is!With no flame we see the steam plumeThe “invisible” flame is low emissivity blue flame
ADDED BENEFIT: No Muffler Needed, No Exposed Steam Jet, No Jet Noise
Need to Get Providence to
Prove Flame is there.
Or a Flame Scanner
Williams.
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FLARE COMBUSTION | PARADIGM SHIFT #2:Water Gas Shift Reaction
4G: Steam Used to Enhance Combustion Reactions
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“Water Gas Shift Reaction”Used by adjacent combustion industries: Thermal Oxidizers, Process burners, Aerospace, etc. recognize that water injection into fuel results in significant combustion improvement and NOX reduction.
GasSteam
KK5
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Slide 13
KK5 Maximize Steam and Hydrocarbon Mixing and minimize steam and air mixingKraus, Kurt, 9/3/2019
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FLARE COMBUSTION | PARADIGM SHIFT #2:Water Gas Shift Reaction
13
4G: Steam Used to Enhance Combustion Reactions
WGSR occurs after carbon monoxide (CO) is formed by partially combusting the hydrocarbons with the reforming reaction (R1):
CnH2n+2 + nH2O nCO + (2n+1) H2 (R1)
This enables WGSR, which is a moderately exothermic reversible reaction expressed by:
CO + H2O CO2 + H2 ΔH0298 = -41.09 kJ/mol (R2)
These reactions (R1) and (R2) are intermediate reactions of the overarching hydrocarbon combustion reaction:
CnH2n+2 + (1½n+1/2)O2 nCO2 + (n+1) H2O (R3)
The reforming products are finally combusted:
H2 + ½O2 H2O (R4)CO + ½O2 CO2 (R5)
But the really interesting mechanisms are happen with the partial products of the WGSR inside the double arrows ‘’ of (R2). It is here where the highly reactive H+ and OH-free radicals are joining the already present and highly reactive CO.
KK1
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Slide 14
KK1 WGSR works within the hydrocarboncombustion process by reducing activation energies,solvating, and catalysing, thereby accelerating thedisassociation of carbon-carbon and carbon-hydrogenbonds. Hydrocarbons, particularly unsaturatedhydrocarbons, are burned more easily, fully and rapidlywith intimately present and thoroughly mixed water.Further, it is much more effective to mix water with thefuel at elevated temperatures than it is to mix steam withair before entering the hydrocarbon stream.Kraus, Kurt, 8/31/2019
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4G VS 3G | PRODUCT COMPARISON MATRIX
*Publicly published S/HC ratios. Smokeless maximum is based on ratio of S/HC to the nViro-XSR.
Note: Smokeless maximum based on a 5 Psig back pressure limit.UOP 8381-14
Feature: Steam Consumption4G
nViro-XSR3G
API 521 Average Reduction
Steam-to-Hydrocarbon Ratio (Propane) 0.12 0.3 60%
Steam-to-Hydrocarbon Ratio (Propylene) 0.18 0.55 67%
Increase Paraffin to Olefin 50% 83%
Feature: Full Range Smokeless Capacity
4GnViro-XSR
3GAPI 521 Average 4G Increase
Vent Gas Flow at Smokeless Maximum/ Maximum Flow (Propane)
100% 22% 354%
Vent Gas Flow at Smokeless Maximum/ Maximum Flow (Propylene)
100% 12% 733%
Across Entire Operating Range: Standby to Full Load
Capacity Loss Olefin to Paraffin 0% 45%
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DIRECT EVIDENCE OF WATER GAS SHIFT REACTION WGSR AT WORK
15
*Publicly published S/HC ratios. Smokeless maximum is based on ratio of S/HC to the nViro-XSR.
Note: Smokeless maximum based on a 5 Psig back pressure limit.
UOP 8381-15
Feature: Full Range Smokeless Capacity
4GnViro-XSR
Steam
4GnViro-XSRNitrogen Increase
Inert-to-Hydrocarbon Ratio(Propane)
0.12 0.16 33%
Inert-to-Hydrocarbon Ratio (Propylene)
0.18 0.25 39%
Standby to Full Load
Increase Paraffin to Olefin 50% 56%
WGSR Works Within the Hydrocarbon Combustion Process By:
• Reducing Activation Energies
• Solvating and Catalyzing
• Thereby Accelerating the Disassociation Of Carbon-Carbon and Carbon-Hydrogen Bonds
Hydrocarbons, particularly unsaturated hydrocarbons, are burned more easily, fully and rapidly when there is intimately present and thoroughly mixed water.
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HOW MUCH IS DUE TO BETTER MIXING, PARADIGM SHIFT #1 VS. WGSR, PARADIGM SHIFT #2
16
*Publicly published S/HC ratios. Smokeless maximum is based on ratio of S/HC to the nViro-XSR.
Note: Smokeless maximum based on a 5 Psig back pressure limit.
UOP 8381-16
Feature
4GnViro-XSR
Steam
4GnViro-XSRNitrogen
3GAPI 521 Average
Due to Mixing- PS1
Due to WGSR- PS2
Inert-to-Hydrocarbon Ratio(Propane)
0.12 0.16 0.30 78% 22%
Inert-to-Hydrocarbon Ratio (Propylene)
0.18 0.25 0.55 81% 19%
Increase Paraffin to Olefin 50% 56% 83%
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4G XSR TECHNOLOGY OPERATING COST
17
Note: Based on average flaring behavior of 2005-2015 SCAQMD refineries with 2 flares assumed and optimal flare selection. OPEX is per flare. Standby steam rate for ‘Competitor’ is assumed based on general practice. Price of Purge Gas [$/MMBtu] $2.93. Steam $0.0033 / 1000lb
0
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3G 1990Inner Steam
2G 1960Upper Steam
Op
era
tin
g C
os
t (U
SD
/Ye
ar)
One Year OPEX Comparison
Visible Emissions Violations [$/yr]
Makeup Gas [$/yr]
Purge Gas [$/yr]
Standby Steam [$/yr]
Smoke Suppressing Steam [$/yr]
UOP 8381-17
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EXCELLENT COLD WEATHER OPERATION: NO ICE BUILDUP ON FLARE TIP | PARADIGM SHIFT #3
18UOP 8381-18
• Steam is Never Mixed with Cold Air Being Pushed Into Flare Tip
• Steam Piping Is Inside the Flare tip, Heating Up Inside the Flare Tip
• No Center Steam
• All Steam Exits the Flare Tip
• Here the steam was run overnight in zero degree weather
• No Assist Gas, Just Steam
• Pilot off
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CALLIDUS NVIRO 4G COMBUSTION TECHNOLOGY REVIEW
19
Up to 67% Less Steam and over 700% Greater Smokeless Means < 1 Year ROI
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Steam, Gas, Jet Technology
Steam, Air Mixing
Technology
Water-Gas Shift
Chemistry
Callidus R&D2016
Callidus IS^3
1990’s
4GTechnology
3G
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CALLIDUS FLARE TECHNOLOGY
Callidus World Class Flare Test Facility
• Process Steam Control
• Drone Inspection Service
• AMEL Multipoint Ground Flare Testing
• RSR Development
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CALLIDUS FLARE TECHNOLOGY
Email: [email protected]
BURNERS PARTS FLARES
Matt McSpadden Debra Wenaas Steve Freimuth
Jesse Chambers Brian Yeates Kurt Kraus
Albert Septiano
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Honeywell Confidential - ©2019 by Honeywell International Inc. All rights reserved. 22Footer, Arial Bold 10pt
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SMART FLARE MONITORING BENEFITS
• Reduce Operator Load in continuously monitoring flare
• Enable multi tasking while enabling efficient flare monitoring
• Help’s Reduce Environmental Non-Compliance Incidents like black smoke • Real time alerts to operator enable faster corrective actions.
• Saves Hours of Manual Efforts in searching videos for events. • Recorded Event Data enable’s analysis & reporting of flare events
Secure and Easy Access to multiple stake holders• Browser based client enable easy access to multi stakeholders – Operations, HSE
23
Enhancing Flare Monitoring Efficiency, Compliance
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HONEYWELL’S AI BASED FLARE MONITORING ANALYTICS
24
Flame Black Smoke Black Cloud
Blue Sky
FlameSteam
Grey Cloud Grey Smoke
Flame
Grey Cloud Black Smoke
Flame
SteamWhite Cloud
Training ( Offline)
Real Time VideoInput
ProcessedOutput
Flame
Steam
Model Learning Update
Feedback Raw Data
Multiple Images of flare used to Train the model
PatentsApplied
Black Smoke
Honeywell’s FLARE AI Model
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FLARE ANALYTICS CHALLENGES
25
Traditional Video Analytics Would Not Work For Flare
• Complex Background (sky color and cloud cover)• Windy conditions• Challenging Lighting Conditions• Low Visibility due to Weather Condition• Continuously Changing Flare Size
Examples of Challenging Scenarios :
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ADVANCED FLARE ANALYTICS
26
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SMART FLARE MONITORING USER INTERFACE
27* This is early version of UI – Functionality may change in final release.
PatentsApplied
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SMART FLARE MONITORING TYPICAL SETUP
Embedded PCWith Advanced Flare analytics
DVM Network
Existing IP camera looking at Flare
Existing DVM Servers
Existing DVM client
Secure Advanced Flare Monitoring
browser client ( Any PC on network )
# Flare Monitoring Components in Red Text
• No disturbance to existing flare monitoring setup and DVM system.
• A parallel stream from the IP camera would be configured in flare analytics box.
• Flare analytics client can be accessed via browser on any PC having access configured to the system.
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Email: [email protected]
BURNERS PARTS FLARES
Matt McSpadden Debra Wenaas Steve Freimuth
Jesse Chambers Brian Yeates Kurt Kraus
Albert Septiano
![Page 34: Training - Day 4 Oct 8 2020 Flare Case Studies...6OLGH .. :*65 ZRUNV ZLWKLQ WKH K\GURFDUERQ FRPEXVWLRQ SURFHVV E\ UHGXFLQJ DFWLYDWLRQ HQHUJLHV VROYDWLQJ DQG FDWDO\VLQJ WKHUHE\ DFFHOHUDWLQJ](https://reader036.fdocuments.us/reader036/viewer/2022062608/606fdd76b7da7c39193a3294/html5/thumbnails/34.jpg)
CASE STUDY:THE GALAXY™MULTIPOINT GROUND FLARE BURNER
October 8, 2020 2020 Combustion SchoolVirtual PresentationUOP 8446-30
TOM RAPPSILBERENGINEERING MANAGER
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GALAXY MULTIPOINT GROUND FLARE BURNER
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GALAXY MULTIPOINT FLARE BURNER
Galaxy Burner Overview:
• Smokeless under all operating conditions
• Extensive destruction efficiency testing
• No visible flame at full load
• Already approved by the EPA for use in Multi-Point Ground Flares
• Pre-Tested for a wide variety of vent gases
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GALAXY ADVANTAGES
Shorter Flame
Higher flow rate reduces the number of burners required
Reduced Heat on Runners increases longevity
Improved Smokeless Performance
Higher Heat Density Reduces Plot Space
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INCREASED FLOW – LOWER FLAME
34
MP-4U Burner 100% Flow New Technology – Galaxy Burner 175% Flow
60’ ELEVATION
45’ ELEVATION
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REDUCED HEAT ON RUNNER
35Footer, Arial Bold 10pt
MP-4U Burner New Technology – Galaxy Burner
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REDUCED PLOT SPACE REQUIREMENTS
36Footer, Arial Bold 10pt
Galaxy Burners Reduce Plot Space by 18%
1000 T/H Flare Field with MP-4U Burners
1000 T/H Flare Field with Galaxy
Burners
230 ft
30
5 f
t
190 ft
30
5 f
t
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REDUCED MULTI-BURNER FLAME LENGTH
Unique patent pending design
Designed to work in conjunction with multiple flare burners as a system.
Designed to maintain flame length as more burners come online
Proven in CFD and testing
37
Flame Length Maintained During High Flow
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REDUCED MULTI-BURNER FLAME LENGTH
Unique patent pending design
Coalesced flame length comparison of a Steam Assisted MP4-UI, and unassisted Galaxy burners in same field.
• 9 Galaxy burners operating at >2X the flow rate as the 3 steam assisted burners, with significantly shorter flame length, at same operating pressure.
38
Flame Length Maintained During High Flow
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IMPROVED SMOKELESS OPERATION
Tested with no smoke at 42% of de-stage pressure on propylene
Allows for fewer burner heads
Reduced chance of smoking
Increases capacity due to wider range of operation
39
Lower Pressure Before Smoke Onset
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REDUCED SINGLE BURNER FLAME LENGTH
At 150% flow rate compared to previous generation of burners the flame is 20% shorter
Tested across multiple vent gas types
40
Shorter Flames Across All Operating Conditions
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GALAXY PERFORMANCE
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No Visible Smoke Performance Testing< 28 kPa Smokeless
Pressure for all wastewith > 99% Confidence
Reliable Ignition with LowNoise
31% Improvement in FlameIgnition Rate at < 1 Second
No Visible Flame
3
2
1
0
4
5
0 .6 0 .7 0 .8 0 .9 1 .0 1 .1
Den
sity
Norma l ized F lame Length
B urner Ga lax y
Previous Generation
Mean StDev 0.81 46 0.08878
1 0.05939
N orm al
Reliable Design FEA Analysisand Minimization of Thermal Stress
8 Shorter FlamePhysical Test andC7 omputer Simulation6
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Q&A42
UOP 8446-42
Email: [email protected]
BURNERS PARTS FLARES
Matt McSpadden Debra Wenaas Steve FreimuthJesse Chambers Brian Yeates Kurt Kraus
Albert Septiano