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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
FLOWSIC100 Flare – Challenges in Ultrasonic Flare meter field installations Mart Gloudemans, Sebastian Stoof, Sven Holzbächer SICK Germany
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
History of Evolution
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
SICK FLOWSIC100 has track record in flare metering since 10 years
Introduction
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014 5
Identifying flare gas measurements
•! Novy Urengoi •! Gas flow measurement at Oil processing
plant •! Ultrasonic flow meter FLOWSIC 600 •! Typical measurement range 0.3 .. 40 m/s •! Meter is out of work
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014 6
Possible reasons: •! Dirty transducers •! High liquid contents •! Noise disturbance •! Electronic or Sensor faults
Identifying flare gas measurements
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014 7
Reason for meter malfunction: •! Typical flare gas application •! Associated petroleum gas •! Velocity of gas approx. 85 m/s •! Blowing away effect
Identifying flare gas measurements
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Waste gas from chemical and petrochemical processes
:! Associated Petroleum Gas from oil exploration
What is flare gas?
Flare gas – the unavoidable by-product
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Flare gas – the unavoidable by-product
Unit A Unit B
Factory IIFactory 1
FT_Q
Challenge: Process waste gases are not emitted directly into the atmosphere.
•! Typical velocity of gas 0.03 .. 1 m/s at ambient pressure
•! Molecular weight is important for leakage detection and process control
•! 95% of process working time velocities < 1 m/s
•! Varying gas composition
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Flare gas – the unavoidable by-product
System depressurizing in emergency situations
•! Significant amounts of gas leads to velocities up to 100 m/s
•! Requirement for avoiding pressure drops
•! High pressure condition
•! Pipe sizes 8“ .. 72“ (200 .. 1800 mm)
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014 18
For emission and CO2 reduction many countries have been defining regulations and standards
•! Annually volume of CO2 certificates emitted by flaring: 370 Mio !
•! APG flaring causes 1.2% of total global CO2
emission •! Russian Government Decree No.344 with
emission fee for flaring of APG
•! Global trend to flare gas recovery
•! There are anti-flaring legislations with defined legal flaring limits + escalating penalties in most countries.
Emission trading of CO2 certificates
COMMISSION DECISION of EG/589/2007
Flare gas measurement – Quo vadis?
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Flare gas measurement – Quo vadis?
For economic and environmental reasons:
:! Recovery of flare gas becomes increasingly important.
:! Various technologies for flare gas recovery available
:! Taxes and fees for flaring of hydrocarbons are raising all over the world
:! CO2 is going to be the most important value for GHG measurements
:! Raising world energy prices makes flaring uneconomical.
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Calculation of CO2 emissions for compliance with government regulations.
:! Monitoring of abnormal process changes.
:! Reduction of gas wastage.
:! Process optimization and accurate mass balance calculation.
:! Optimization of steam usage.
Purpose of flare gas measurement
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014 21
•! Gas velocity 0.03 .. 120 m/s
•! Extraordinary low flow performance required
•! No pressure drop allowed
•! Contamination by liquids and pollutions
•! Strong variation of gas mixtures
•! Harsh ambient conditions
Challenge of flare gas measurement
Turn-down ratio 4000 : 1
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
1.! Low flow performance To fulfill process optimization task and identification of valve leakage
Requirements on the flaregas measurement
2.! High flow measurement Availability of measurement in shutdown conditions.
3.! Measurement availability in “difficult” gas compositions Light + heavy gas. Sound absorbing gas.
4.! Adapted installation capabilities Long-term plant operation. Limited accessibility to piping. (Extraction Tools) Offshore installation.
Challenges of flaregas metering – The measurements companies view
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Very unstable flow conditions + backflow.
Challenge 1: “Low Flow” condition < 1 m/s
:! Strong reduced measuring effect –
smallest transit time difference.
:! Thermal stratifications.
Extreme stability requirements
Operation in low flow conditions
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
1.! Time resolution
:! System +/-5ns in practise conditions
SICK transducer technology
2.! Measurement stability, ensured by:
:! Precise transducer signals
:! “Broadband” system
:! Highly accurate signal algorithm
:! Highly stable elctronics
3.! Special verification procedure for zero point stability
Operation in low flow conditions
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
SICK Performance verification using special zero flow check
Operation in low flow conditions
Trend VOG [m/s]
-0,001
-0,0005
0
0,0005
0,001
0 50 100 150 200
Time [s]
Zero flow stability of 0.6 mm/s
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Several local regulations recommends a meter performance check every year
Field verification procedure needed
:! Field test box:
-! On-site capable
-! Zero point adjustment
-! Factory standard
SICK field verification of meter
Operation in low flow conditions
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Closed box with minimal influence of temperature and fluctuations
SICK field verification of meter
Operation in low flow conditions
:! Data acquisition and evaluation with FLOWSIC FAD tool
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Signal is „blown away“, received signal amplitudes
are reduced
:! Signal beam – an optimization task
-!Wider signal beam angle distributes energy over a
larger area
-! Small signal beam might not hit the receiving
sensor
“High Flow” condition 100 m/s or more
:! Disturbing noise in the pipeline and at the sensor
Limited Signal Noise Ratio (SNR)
Challenge 2: Operation in high flow conditions
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Investigations in Signal Noise Ratio (SNR)
Noise Level undisturbed flow 80 kHzp ambient
0
50
100
150
200
250
300
0 10 20 30 40 50 60 70 80 90 100 110 120
VOG [m/s]
Rec
eivi
ng A
mpl
itude
[dig
it]
Sensor B
Sensor A
The sensor inside the gas flow becomes to a significant source of noise !
Operation in high flow conditions
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Aerodynamic probe design
•! Probe design with ultrasonic sensor embedded in an aerodynamic shape
•! Noise reduction at sensor – Significant improvement of Signal Noise Ratio (SNR)
•! Path angle of 75°
Operation in high flow conditions
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Probe design with ultrasonic sensor embedded in an aerodynamic shape
A
B
SICK innovative high speed sensor design
:! Noise reduction at sensor – Significant improvement of Signal Noise Ratio (SNR)
Operation in high flow conditions
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Short term changes possible.
Challenge 3: Gas composition
:! Difficult compositions can reduce SNR by a changed transmission
characteristics of transducers.
Considerations for gas composition
Light gas
SOS ~700 m/s
Sound beam lobe
Heavy gas
SOS ~280 m/s
Natural gas
SOS ~400 m/s
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
SICK transducers + signal algorithm
SOS 934 m/s, MW 3.5 g/mol, ~90%H2, 10% CH4
SOS 611 m/s, MW 7.8 g/mol, ~60%, 40% CH4
SOS 349 m/s, MW 23 g/mol
:! Transducers with large bandwidth and amplitudes ! gas composition do not have a significant effect on signal performance.
:! SICK Flare measurement starting at compositions with MW 2 g/mol.
Considerations for gas composition
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
2-path configuration
:! Much less sensitive for flow profile deformations at instable flow conditions
:! 2-path meter can reduce uncertainty down to 1 %
Meter installation requirements
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Optional 2-path configuration :! For higher accuracy demands. :! For representative measurement results also under difficult measuring conditions
(disturbed flow, gas composition).
Meter installation requirements
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Gas with liquids and pollutions
:! Use of high power version FLOWSIC100 Flare EX-RE
Meter installation requirements
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
1.! Device without meter body :! Hot tapping installation
:! Nozzle installation tool / geometry calculator
:! 1- or 2-path configuration
Meter installation requirements
Solutions: Flowmeter with and without meter body
2.! Device with meter body :! System solution - plug&play
:! Factory-sided parameterization - ready for operation
:! Solution for higher uncertainty demands by optional:
:! Highly precise 3D survey
:! Flow calibration for uncertainty down to 0.5%
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
!! < +/- 0.1 mm
Meter body
3D survey - Minimizing geometric uncertainty
Meter installation requirements
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Calibration on SICK test stand, approved and traceable to national standard, represented by the german PTB (Physikalisch Technische Bundesanstalt, Germany).
:! Test benches is equipped with two electric fans with a total connected power of 70 kW.
Measurement range 30 ! 13000 m"/h
Optional flow calibration
Meter installation requirements
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Offshore installations :! Highly robust device configuration with electronics housings in stainless steel :! Highly durable material configurations in Duplex or Hastelloy :! Special paintings
Meter installation requirements
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014 64
Business opportunities
Example Offshore platform Norway
•! Mass flow: ~ 165.844 t/year •! Emission: ~ 500.000t CO2/year
CO2 tax Norway: 21$ /CO2 t (15!/ CO2 t) Costs CO2 Emission total: 7.5 Mio !/year 1% accuracy increase: 75.000 !/year per plant
Case Mass flow Annually
Min 160 t/h 95%
Normal 290 t/h 3%
Max 504 t/h 2%
Total amounts:
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
FLOWSIC100 Flare – solutions
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Optional 3x1path configuration :! System solution to serve 3 different flare measurements with a single control unit.
Flare 1
Flare 3
Flare 2
Meter installation requirements
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Remote installation of control unit up to 1,000 m (3,000 ft) from measurement location
Meter installation requirements
:! Installation of control unit in safe area.
:! Safe costs of an expensive installation in hazardous area.
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Single-sided installation :!Use of “probe version” FLOWSIC100 EX-PR
up to 1,000 m
Control unit non-ex or Ex-Zone 1 and 2 (ATEX), Cl I, Div2 (CSA)
Safe or hazardous area
Meter installation requirements
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
FLOWSIC100 EX-S FLOWSIC100 EX FLOWSIC100 EX-PR -! „Standard“ cross-duct - Retractable - ATEX Zone 1+2 -! CSA Cl I, Div.1/2 -! IEC Ex Ga/Gb Ex d [ia] IIC T4
-! „High power“ cross-duct - Retractable - ATEX Zone 1+2 -! CSA Cl I, Div.1/2 -! IEC Ex Ex d IIC T4
-! Probe version - Retractable - ATEX Zone 1+2 -! CSA Cl I, Div.1/2 -! IEC Ex Ga/Gb Ex d [ia] IIC T4
FLOWSIC100 Flare – Operation principle & devices
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Medium housing -! non-ex
-! ATEX Ex zone 2
-! CSA Cl I, Div2 / zone 2
-! up to 3 measurement points -! optional conduit connection
:! Flameproof housing
-! ATEX Ex zone 1 -! up to 3 measurement points
-! optional conduit connection
Multi Control Unit MCUP
FLOWSIC100 Flare – Operation principle & devices
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Conclusion
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
Conclusion
:! Leading transducer technology
•! Best signal performance, shortest time resolution for reliable and precise measurement also in difficult gas conditions.
•! Cross-duct measurement up 72” pipe size.
Trend VOG [m/s]
-0,001
-0,0005
0
0,0005
0,001
0 50 100 150 200
Time [s]
:! Unique zero flow performance verified by special Zero Flow Test procedure.
•! Fast and reliable process control + optimization.
:! Innovative high speed sensor design
•! High measurement availability also in “High flow” conditions up to 120 m/s.
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Installation advantages:
•! 1x1, 2x2 or 3x1 path configuration
•! Remote installation of control unit up to 1,000 m from measurement location Installation in safe area safes costs of an expensive installation in hazardous area.
•! Probe version for single flange mounting Single nozzle installation for pipes with access from one side only. Lowest installation expenditure.
Conclusion
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FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
FLOWSIC100 Flare WIB Meeting, 04/2011 CEESI Flow Measurement Workshop 2014
:! Thank you for your attention.