SlideShare una empresa de Scribd logo
1 de 2
Descargar para leer sin conexión
FEATURE
22 Jurutera, May 2008
Offshore platforms contain hydrocarbon
inventory at the process areas. It is
a hazardous workplace. When there is a
liquid or gas leak, it can harm the people
workingontheplatform.Itwillalsospoilthe
equipment and damage the environment.
A fire and gas detection system is
required on a platform to protect the
personnel, equipment and the fishes
or natural wildlife in the sea. When a
catastrophiceventoccurs,itwillbereported
in the media. It will cost the operator a
lot of money to rectify the problem. It is
worthwhile investing in a fire and gas
solution due to the aforementioned reason.
A fire and gas detection system consists
of field devices that detect a gas leak or a
fire when it develops. It will then send a
signal to a control system which will then
sound the alarm and isolate the supply of
hydrocarbon inventory flowing into the
platform. When this happens, the platform
should be safe from a catastrophic event
because the source of the hydrocarbon has
been stopped. The power supply is also
isolated to these areas.
The danger is when the safeguarding
system fails to work, i.e. when it is
supposed to activate the alarm, isolate the
power supply and shutdown the platform.
To mitigate this from happening, two gas
detectors or flame detectors are required.
When one fails to work, the other is able to
step in.
When a detection system is in place, a
lot of money can be saved. People can work
safely on a platform. Equipment will be
protected and will not be severely damaged.
The harm to the environment is minimised.
However, ensuring the safety of
personnel on a platform is not easy. The idea
of prevention is important because if there is
a leak, it must be stopped. Hence, a fire and
gas detection system is required to prevent
this from happening, thus people working
on a platform are able to avoid the danger.
What are the chances of a leak occurring
at the same time when a person is working
at a hazardous area? As such,
a model to predict such an
occurrence is required. In the
later section, it is suggested
that the fire and gas detection
system need to be reliable and
safe. A quantitative approach
is also suggested, based on two
equations,toavoidacatastrophic
occurrence.
Reliable and Safe
Detectors – What
does it mean?
Fire and gas detection in the oil
andgasindustryrequiresreliable
and safe detectors. Some of the
elementsthatconstituteareliable
and safe detector are built-in
quality (which includes product
assurance), high operation
performance (minimum faults
or failure; if possible, zero
breakdown) and best possible
components – source from
prominent suppliers.
Operation Performance
The detectors must function all the
time to transmit signal to the detection
system when there is a fire or leak, e.g.
gas, flame or smoke. Failure will result in
poor performance. Fault alarms must be
generated in the system when detectors in
thefieldfailtooperate.Performanceisrated
by identifying the number of failures.
Built-in Quality
A manufacturer has to realise that quality
is important. Built-in quality is regarded
as an organisation with a quality system in
place, a group of resourceful people, etc.
Quality is free, according to top quality
gurus. Achieving this is a challenge.
Best Possible Suppliers
Component suppliers must supply good
components that will last a long time.
The electronic devices must be sourced
from a good electronics maker, in order
to produce a reliable and safe detector
required by customers. Suppliers need to
look out for the best component supplier
which will contribute indirectly to the
performance of the detectors.
Failure Rate and Mean
Time Between Failure – A
Quantitative Measure of
Safe Operations
The failure rate is an equation to calculate
thenumberoffailuressentouttocustomers
over the total number of production
output. This is an equation to know how
well is the device being manufactured.
Mean time between failures is another
equation that is used to calculate the
actual number of failures in use by the
customers over a period of time. It is
Figure 1: Diagram of a redundant processor
Figure 2: The challenge to achieve a reliable and safe detector
Fire and Gas Detection –
A Safeguarding System Worth Investing
..........................................................................................................................................................................................................................
By: Ir. Gan Chun Chet
(To be continued at page 24)
FEATURE
24 Jurutera, May 2008
an equation to determine the duration
between failures collected throughout
the use of the device. Statistically, this
number will depict an estimate time of an
actual failure that is going to happen.
Failure Rate = X 100
Mean Time Between Failure (MTBF)
=
T = Operation Duration
F = Repair Duration
|------T1----||---F1----||-------T2------||----
F2---|...|---TN---||---FN---|
Mean or Average Time Between Failures
=
In the case of gas and flame detectors,
this number is dependent on the fire and
gas suppliers. And for every supplier, it is
different in every case.
In fire and gas detection, the time of an
actual failure taking place in a field device
is unknown. Only an estimate can be
determined. The number of the detectors’
failure rate is important because if this figure
is high, it means that the quality is bad.
Inversely,ifthefailurerateislow,thismeans
that the quality of the product is good.
The quantitative calculation is to
determine whether there is a repeat case
of failure. If it does not recur, then the
incident could be sporadic. In which case,
an analysis is required on the collected
data. Limits might then be applied.
As an additional point, the platform
needs to be well maintained to avoid an
incident from occurring. Proper predictive
tools to monitor the performance of pumps
or compressors are required. Regular visual
checks on the condition of a platform are
also required to ensure that the machinery
and equipment are well maintained. n
Theauthorisapracticingprofessionalengineer
with a contractor/consultant company in the
oil and gas industry based in Kuala Lumpur.
References
[1]	 Operations Management, Nigel
Slack, Stuart Chambers, Christine
Harland, Alan Harrison and Robert
Johnston, Pitman Publishing, 1995.
[2]	 Managing Quality, Edited by Barrie
G. Dale, Prentice Hall, 1994.
Number of Failures
Total Number of
Products Tested
Operating Hours
Number of Failures
T1 + T2 + .........TN
N

Más contenido relacionado

Más de Gan Chun Chet

Fire and Gas Detection System : Part 1_The Field Devices and Its Panels
Fire and Gas Detection System : Part 1_The Field Devices and Its PanelsFire and Gas Detection System : Part 1_The Field Devices and Its Panels
Fire and Gas Detection System : Part 1_The Field Devices and Its PanelsGan Chun Chet
 
Trust Measurement Presentation_2.pptx
Trust Measurement Presentation_2.pptxTrust Measurement Presentation_2.pptx
Trust Measurement Presentation_2.pptxGan Chun Chet
 
Boundary Layer Oscillation for Aircraft Cavity/Surfaces
Boundary Layer Oscillation for Aircraft Cavity/SurfacesBoundary Layer Oscillation for Aircraft Cavity/Surfaces
Boundary Layer Oscillation for Aircraft Cavity/SurfacesGan Chun Chet
 
Noise dB to dBA Calculation_Gan Chun Chet.pptx
Noise dB to dBA Calculation_Gan Chun Chet.pptxNoise dB to dBA Calculation_Gan Chun Chet.pptx
Noise dB to dBA Calculation_Gan Chun Chet.pptxGan Chun Chet
 
Noise Error Calculation_Gan Chun Chet.pptx
Noise Error Calculation_Gan Chun Chet.pptxNoise Error Calculation_Gan Chun Chet.pptx
Noise Error Calculation_Gan Chun Chet.pptxGan Chun Chet
 
Noise_Proofing Linking Equations.pdf
Noise_Proofing Linking Equations.pdfNoise_Proofing Linking Equations.pdf
Noise_Proofing Linking Equations.pdfGan Chun Chet
 
The Prediction of Time Trending Techniques in Manufacuturing
The Prediction of Time Trending Techniques in ManufacuturingThe Prediction of Time Trending Techniques in Manufacuturing
The Prediction of Time Trending Techniques in ManufacuturingGan Chun Chet
 
The Philosophy and Characteristics of Trust Measurement in Practice.docx
The Philosophy and Characteristics of Trust Measurement in Practice.docxThe Philosophy and Characteristics of Trust Measurement in Practice.docx
The Philosophy and Characteristics of Trust Measurement in Practice.docxGan Chun Chet
 
Trust Measurement Gan Chun Chet 07.01.2022
Trust Measurement Gan Chun Chet 07.01.2022Trust Measurement Gan Chun Chet 07.01.2022
Trust Measurement Gan Chun Chet 07.01.2022Gan Chun Chet
 
mV to dBm Airflow Across Cavity_Gan Chun Chet_07.01.2021
mV to dBm Airflow Across Cavity_Gan Chun Chet_07.01.2021mV to dBm Airflow Across Cavity_Gan Chun Chet_07.01.2021
mV to dBm Airflow Across Cavity_Gan Chun Chet_07.01.2021Gan Chun Chet
 
Control System_3rd Order System_Root Locus Method
Control System_3rd Order System_Root Locus MethodControl System_3rd Order System_Root Locus Method
Control System_3rd Order System_Root Locus MethodGan Chun Chet
 
PID Controllers Control Engineering
PID Controllers Control EngineeringPID Controllers Control Engineering
PID Controllers Control EngineeringGan Chun Chet
 
Noise Reduction Modelling Study for Aircraft Cavity - Chun C Gan
Noise Reduction Modelling Study for Aircraft Cavity  - Chun C GanNoise Reduction Modelling Study for Aircraft Cavity  - Chun C Gan
Noise Reduction Modelling Study for Aircraft Cavity - Chun C GanGan Chun Chet
 
Calculation worksheet air flow across rectangular cavity low mach
Calculation worksheet air flow across rectangular cavity low machCalculation worksheet air flow across rectangular cavity low mach
Calculation worksheet air flow across rectangular cavity low machGan Chun Chet
 
Noise Error Calculation : Averaging and Industrial Standards (Formula)
Noise Error Calculation : Averaging and Industrial Standards (Formula)Noise Error Calculation : Averaging and Industrial Standards (Formula)
Noise Error Calculation : Averaging and Industrial Standards (Formula)Gan Chun Chet
 
Fluid dynamics 02 tank control system single_cascade
Fluid dynamics 02 tank control system single_cascadeFluid dynamics 02 tank control system single_cascade
Fluid dynamics 02 tank control system single_cascadeGan Chun Chet
 
Fluid dynamics 01 flow elements oriflce plate control valve
Fluid dynamics 01 flow elements oriflce plate control valveFluid dynamics 01 flow elements oriflce plate control valve
Fluid dynamics 01 flow elements oriflce plate control valveGan Chun Chet
 
Air Flow Across Cavities (Aircraft Industry) - Gan Chun Chet
Air Flow Across Cavities (Aircraft Industry) - Gan Chun ChetAir Flow Across Cavities (Aircraft Industry) - Gan Chun Chet
Air Flow Across Cavities (Aircraft Industry) - Gan Chun ChetGan Chun Chet
 
Noise Prediction_Prevention : An industrial Calculation Approach - Ir. Gan Ch...
Noise Prediction_Prevention : An industrial Calculation Approach - Ir. Gan Ch...Noise Prediction_Prevention : An industrial Calculation Approach - Ir. Gan Ch...
Noise Prediction_Prevention : An industrial Calculation Approach - Ir. Gan Ch...Gan Chun Chet
 
The Prediction Of Time Trending Techniques. Is It A Reasonable Estimate?
The Prediction Of Time Trending Techniques. Is It A Reasonable Estimate?The Prediction Of Time Trending Techniques. Is It A Reasonable Estimate?
The Prediction Of Time Trending Techniques. Is It A Reasonable Estimate?Gan Chun Chet
 

Más de Gan Chun Chet (20)

Fire and Gas Detection System : Part 1_The Field Devices and Its Panels
Fire and Gas Detection System : Part 1_The Field Devices and Its PanelsFire and Gas Detection System : Part 1_The Field Devices and Its Panels
Fire and Gas Detection System : Part 1_The Field Devices and Its Panels
 
Trust Measurement Presentation_2.pptx
Trust Measurement Presentation_2.pptxTrust Measurement Presentation_2.pptx
Trust Measurement Presentation_2.pptx
 
Boundary Layer Oscillation for Aircraft Cavity/Surfaces
Boundary Layer Oscillation for Aircraft Cavity/SurfacesBoundary Layer Oscillation for Aircraft Cavity/Surfaces
Boundary Layer Oscillation for Aircraft Cavity/Surfaces
 
Noise dB to dBA Calculation_Gan Chun Chet.pptx
Noise dB to dBA Calculation_Gan Chun Chet.pptxNoise dB to dBA Calculation_Gan Chun Chet.pptx
Noise dB to dBA Calculation_Gan Chun Chet.pptx
 
Noise Error Calculation_Gan Chun Chet.pptx
Noise Error Calculation_Gan Chun Chet.pptxNoise Error Calculation_Gan Chun Chet.pptx
Noise Error Calculation_Gan Chun Chet.pptx
 
Noise_Proofing Linking Equations.pdf
Noise_Proofing Linking Equations.pdfNoise_Proofing Linking Equations.pdf
Noise_Proofing Linking Equations.pdf
 
The Prediction of Time Trending Techniques in Manufacuturing
The Prediction of Time Trending Techniques in ManufacuturingThe Prediction of Time Trending Techniques in Manufacuturing
The Prediction of Time Trending Techniques in Manufacuturing
 
The Philosophy and Characteristics of Trust Measurement in Practice.docx
The Philosophy and Characteristics of Trust Measurement in Practice.docxThe Philosophy and Characteristics of Trust Measurement in Practice.docx
The Philosophy and Characteristics of Trust Measurement in Practice.docx
 
Trust Measurement Gan Chun Chet 07.01.2022
Trust Measurement Gan Chun Chet 07.01.2022Trust Measurement Gan Chun Chet 07.01.2022
Trust Measurement Gan Chun Chet 07.01.2022
 
mV to dBm Airflow Across Cavity_Gan Chun Chet_07.01.2021
mV to dBm Airflow Across Cavity_Gan Chun Chet_07.01.2021mV to dBm Airflow Across Cavity_Gan Chun Chet_07.01.2021
mV to dBm Airflow Across Cavity_Gan Chun Chet_07.01.2021
 
Control System_3rd Order System_Root Locus Method
Control System_3rd Order System_Root Locus MethodControl System_3rd Order System_Root Locus Method
Control System_3rd Order System_Root Locus Method
 
PID Controllers Control Engineering
PID Controllers Control EngineeringPID Controllers Control Engineering
PID Controllers Control Engineering
 
Noise Reduction Modelling Study for Aircraft Cavity - Chun C Gan
Noise Reduction Modelling Study for Aircraft Cavity  - Chun C GanNoise Reduction Modelling Study for Aircraft Cavity  - Chun C Gan
Noise Reduction Modelling Study for Aircraft Cavity - Chun C Gan
 
Calculation worksheet air flow across rectangular cavity low mach
Calculation worksheet air flow across rectangular cavity low machCalculation worksheet air flow across rectangular cavity low mach
Calculation worksheet air flow across rectangular cavity low mach
 
Noise Error Calculation : Averaging and Industrial Standards (Formula)
Noise Error Calculation : Averaging and Industrial Standards (Formula)Noise Error Calculation : Averaging and Industrial Standards (Formula)
Noise Error Calculation : Averaging and Industrial Standards (Formula)
 
Fluid dynamics 02 tank control system single_cascade
Fluid dynamics 02 tank control system single_cascadeFluid dynamics 02 tank control system single_cascade
Fluid dynamics 02 tank control system single_cascade
 
Fluid dynamics 01 flow elements oriflce plate control valve
Fluid dynamics 01 flow elements oriflce plate control valveFluid dynamics 01 flow elements oriflce plate control valve
Fluid dynamics 01 flow elements oriflce plate control valve
 
Air Flow Across Cavities (Aircraft Industry) - Gan Chun Chet
Air Flow Across Cavities (Aircraft Industry) - Gan Chun ChetAir Flow Across Cavities (Aircraft Industry) - Gan Chun Chet
Air Flow Across Cavities (Aircraft Industry) - Gan Chun Chet
 
Noise Prediction_Prevention : An industrial Calculation Approach - Ir. Gan Ch...
Noise Prediction_Prevention : An industrial Calculation Approach - Ir. Gan Ch...Noise Prediction_Prevention : An industrial Calculation Approach - Ir. Gan Ch...
Noise Prediction_Prevention : An industrial Calculation Approach - Ir. Gan Ch...
 
The Prediction Of Time Trending Techniques. Is It A Reasonable Estimate?
The Prediction Of Time Trending Techniques. Is It A Reasonable Estimate?The Prediction Of Time Trending Techniques. Is It A Reasonable Estimate?
The Prediction Of Time Trending Techniques. Is It A Reasonable Estimate?
 

Fire and Gas Detection - A Safeguarding System Worth Investing

  • 1. FEATURE 22 Jurutera, May 2008 Offshore platforms contain hydrocarbon inventory at the process areas. It is a hazardous workplace. When there is a liquid or gas leak, it can harm the people workingontheplatform.Itwillalsospoilthe equipment and damage the environment. A fire and gas detection system is required on a platform to protect the personnel, equipment and the fishes or natural wildlife in the sea. When a catastrophiceventoccurs,itwillbereported in the media. It will cost the operator a lot of money to rectify the problem. It is worthwhile investing in a fire and gas solution due to the aforementioned reason. A fire and gas detection system consists of field devices that detect a gas leak or a fire when it develops. It will then send a signal to a control system which will then sound the alarm and isolate the supply of hydrocarbon inventory flowing into the platform. When this happens, the platform should be safe from a catastrophic event because the source of the hydrocarbon has been stopped. The power supply is also isolated to these areas. The danger is when the safeguarding system fails to work, i.e. when it is supposed to activate the alarm, isolate the power supply and shutdown the platform. To mitigate this from happening, two gas detectors or flame detectors are required. When one fails to work, the other is able to step in. When a detection system is in place, a lot of money can be saved. People can work safely on a platform. Equipment will be protected and will not be severely damaged. The harm to the environment is minimised. However, ensuring the safety of personnel on a platform is not easy. The idea of prevention is important because if there is a leak, it must be stopped. Hence, a fire and gas detection system is required to prevent this from happening, thus people working on a platform are able to avoid the danger. What are the chances of a leak occurring at the same time when a person is working at a hazardous area? As such, a model to predict such an occurrence is required. In the later section, it is suggested that the fire and gas detection system need to be reliable and safe. A quantitative approach is also suggested, based on two equations,toavoidacatastrophic occurrence. Reliable and Safe Detectors – What does it mean? Fire and gas detection in the oil andgasindustryrequiresreliable and safe detectors. Some of the elementsthatconstituteareliable and safe detector are built-in quality (which includes product assurance), high operation performance (minimum faults or failure; if possible, zero breakdown) and best possible components – source from prominent suppliers. Operation Performance The detectors must function all the time to transmit signal to the detection system when there is a fire or leak, e.g. gas, flame or smoke. Failure will result in poor performance. Fault alarms must be generated in the system when detectors in thefieldfailtooperate.Performanceisrated by identifying the number of failures. Built-in Quality A manufacturer has to realise that quality is important. Built-in quality is regarded as an organisation with a quality system in place, a group of resourceful people, etc. Quality is free, according to top quality gurus. Achieving this is a challenge. Best Possible Suppliers Component suppliers must supply good components that will last a long time. The electronic devices must be sourced from a good electronics maker, in order to produce a reliable and safe detector required by customers. Suppliers need to look out for the best component supplier which will contribute indirectly to the performance of the detectors. Failure Rate and Mean Time Between Failure – A Quantitative Measure of Safe Operations The failure rate is an equation to calculate thenumberoffailuressentouttocustomers over the total number of production output. This is an equation to know how well is the device being manufactured. Mean time between failures is another equation that is used to calculate the actual number of failures in use by the customers over a period of time. It is Figure 1: Diagram of a redundant processor Figure 2: The challenge to achieve a reliable and safe detector Fire and Gas Detection – A Safeguarding System Worth Investing .......................................................................................................................................................................................................................... By: Ir. Gan Chun Chet (To be continued at page 24)
  • 2. FEATURE 24 Jurutera, May 2008 an equation to determine the duration between failures collected throughout the use of the device. Statistically, this number will depict an estimate time of an actual failure that is going to happen. Failure Rate = X 100 Mean Time Between Failure (MTBF) = T = Operation Duration F = Repair Duration |------T1----||---F1----||-------T2------||---- F2---|...|---TN---||---FN---| Mean or Average Time Between Failures = In the case of gas and flame detectors, this number is dependent on the fire and gas suppliers. And for every supplier, it is different in every case. In fire and gas detection, the time of an actual failure taking place in a field device is unknown. Only an estimate can be determined. The number of the detectors’ failure rate is important because if this figure is high, it means that the quality is bad. Inversely,ifthefailurerateislow,thismeans that the quality of the product is good. The quantitative calculation is to determine whether there is a repeat case of failure. If it does not recur, then the incident could be sporadic. In which case, an analysis is required on the collected data. Limits might then be applied. As an additional point, the platform needs to be well maintained to avoid an incident from occurring. Proper predictive tools to monitor the performance of pumps or compressors are required. Regular visual checks on the condition of a platform are also required to ensure that the machinery and equipment are well maintained. n Theauthorisapracticingprofessionalengineer with a contractor/consultant company in the oil and gas industry based in Kuala Lumpur. References [1] Operations Management, Nigel Slack, Stuart Chambers, Christine Harland, Alan Harrison and Robert Johnston, Pitman Publishing, 1995. [2] Managing Quality, Edited by Barrie G. Dale, Prentice Hall, 1994. Number of Failures Total Number of Products Tested Operating Hours Number of Failures T1 + T2 + .........TN N