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South East Asia Flow Measurement Conference
3 – 4 March 2015
Technical Paper
1
WHAT WE HAVE LEARNT FROM GC CONDITIONAL BASED
MONITORING
Anwar Sutan, i-Vigilant Technologies
1 Introduction
Online gas chromatograph (GC) is frequently used within fiscal and custody transfer
measurement systems. The accuracy of the analysis from the GC is of the utmost
importance since the resultant analysis is frequently used as the core parameter in
economic transactions.
The modern GC is an extremely repeatable device. However, sources of measurement
error do not always arise from the GC itself. More frequently errors appear due to non-
representative sample provided by the sampling system. Ensuring accuracy and
repeatability of the system requires that suitable monitoring and maintenance is in place.
From GC point of view, even though it may be repeatable, it does not preclude the system
from the possibility of systematic errors. These may include, among others, poor
calibration gas handling resulting in non-homogeneous reference mixture; unsuitable
selection of reference mixture resulting in biases due to linearity or the assumed response
functions; peak drifts; valves leakage etc. One case study shows that in a situation where
systematic error remains undetected, it resulted in an on-going error in the calorific value
of up to 1.4%. Seemingly insignificant on surface, in monetary terms this 1.4% is equated
to a value of more than £300,000 per month.
Assuming reasonable steps have been taken to eliminate systematic errors in GC, it is
essential that sampling and conditioning systems are accordingly verified. Often GC itself
measures correctly, however if the sampling and conditioning system fails to provide
representative gas sample, there would consequently occur a measurement error. Another
case study by the author reveals a situation where heavy end drop out in a system caused
a systematic error with value equated to more than £200,000 per month.
Once it is proved that GC is healthy and sampling system provides representative sample,
then GC measurement uncertainty can be calculated. This paper presents several case
studies that have been performed on various GC. The studies look at the GC current
maintenance regime, then it proposes new ideas for GC maintenance using a conditional
based monitoring tool which monitors all GC calibration parameters to ensure GC
instantaneous correctness. Further analysis of the data allows determination of the
uncertainty of the GC.
The studies performed looked into the comparison between spot sampling and GC reading.
Spot sampling at line pressure can help detect heavy end drop out within the pressure
letdown system. Knowing the long term history of gas composition in the pipeline helps to
identify the stability of the gas and determine the most appropriate gas mixtures to be
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Technical Paper
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used in calibration. Where the gas composition in a pipeline is stable, independent GC
multilevel calibration may not be essential.
Overall, this paper presents a novel philosophy for determining initial health of the GC,
health of the sample let down system and for the continued monitoring and assessment
of both GC and sample conditioning system performance. The goal being to provide on-
line estimates of the repeatability of each component thereby allowing uncertainty
calculations to be performed for calorific value and density (or any other parameter that
can be calculated from gas composition). The philosophy will be demonstrated based on
real data obtained from several case studies. The paper will illustrate how an ‘expert
system’ may be used to provide uncertainty of the GC as well as provide early fault
indication. Therefore, the system would provide assurance that GC is operating within
specified limits and meeting contractual obligations.
2 Conventional GC Maintenance Regime
2.1 Sample let down system
GC is a device that is designed to measure gas composition at near atmospheric pressure;
therefore it is necessary to bring the pressure down from the pipeline pressure to around
2 Barg where the GC operates as illustrated in Figure 1.
Figure 1. Sample pressure let down system illustration
Dropping gas pressure will also drop the temperature of the gas (known as the Joule-
Thomson effect); this brings a risk for the gas to fall into dual phase as the gas
temperature drops below its dew point temperature within phase envelope as shown in
Figure 2 below.
Note: Joule-Thomson effect is the change in temperature that accompanies expansion of
a gas without production of work or transfer of heat [6]. Every 1 bar pressure drop the
temperature will drop as well by approximately 0.5 deg C.
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Technical Paper
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Figure 2. Phase envelope with pressure drop simulation
On an analyser system, it is important to provide representative sample. This means the
gas that is sampled from the pipeline has the same composition as the gas that is injected
to the analyser. If the gas during the pressure drop enters a dual phase region, some of
the gas will change phase into liquid and will be knocked out by filters. In this case the
gas injected to the GC will not be representative of the gas in the pipeline.
This is a challenge that is normally faced by the cold region such as the North Sea.
Therefore the design of the sample let down system always considers the cricondentherm
temperature of the gas to ensure that the gas will never enter the dual phase region within
the phase envelope. The simplified design of sample let down system is illustrated in Figure
3 below.
Figure 3. Typical sample let down system design
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As shown in Figure 3, every piece of sample line must have either heat tracing or heated
elements to ensure that the temperature will be high enough for the gas to remain on the
gaseous phase. It is normal to have two stages of pressure drop to ensure that
temperature remains higher than dew point temperature as illustrated in Figure 4.
Figure 4. Illustration of pressure drop with two stages of pressure drop
ISO 10715:2001 [2] standard specify that to ensure gaseous stage, temperature within
sample system needs to be maintained 10 deg C above dew point temperature.
This means that this issue is not isolated for the cold area. Poor design of sample let down
system can also bring similar issues in warm areas such as South-East Asia. A case been
encountered where only single stage pressure let down is implemented and icing in the
regulator has happened. In this case most likely the gas within the sample system would
have gone into dual phase and a non-representative sample injected to the GC.
The issue of heavy end drop out is important with large financial implication for the
operator. A case study was done in the UK where more than 50% of drop out in the heavy
end occurred (i.e. 0.1% C7+ was measured by GC while spot sampling shows in average
around 0.25% C7+ should have been measured). This contribute to 0.75% of a mis-
measurement. Dependent on the volume of the gas flowing this can worth more than
£100,000.00 /month of error.
Therefore sample let down system design should not be taken lightly, analysis of the gas
by comparing spot sampling result against GC result needs to be taken, and when heavy
end drop out is detected necessary actions need to be taken.
2.2 Calibration Gas and Calibration Process
Calibration gas on gas chromatography is very important. The accuracy of GC
measurement is dependent on the accuracy of the calibration gas. The uncertainty of GC
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Technical Paper
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measurement, among other things, is affected by how close the calibration gas represents
the pipeline gas and the uncertainty of the calibration gas. Wrong selection of calibration
gas and faults in calibration process have proven to be sources of significant error in GC
measurement.
Issues in calibration gas or calibration process will not be detected by having redundant
GC as both GC will experience the same issue and have the same systematic error that
can go undetected. The following are some of the issues that have been encountered with
calibration gas or calibration process in the GC.
1. High uncertainty of calibration gas
In a measurement system, accuracy is at the utmost importance. Calibration gas that is
made with high uncertainty will result in high uncertainty GC measurement result. This
may lead to less confidence in GC measurement. To ensure the most accurate
measurement, calibration gas needs to be made with the most accurate method aiming at
the lowest uncertainty possible.
As an example, as illustrated in Table 1 below, the calibration gas that is made with higher
accuracy only contribute to overall CV uncertainty of 0.03% while calibration gas that is
made with uncertainty of ±2% on all components contribute to 0.15% of CV uncertainty.
This lead to low confidence of GC measurement, furthermore the use of poor calibration
gas may bring the overall system uncertainty out with the allowable metering system
uncertainty budget.
Description High accuracy uncertainty 2% uncertainty
Methane 0.0352 % 2 %
Nitrogen 0.3259 % 2 %
CO2 0.2506 % 2 %
Ethane 0.2801 % 2 %
Propane 0.3327 % 2 %
i-Butane 0.3205 % 2 %
n-Butane 0.3742 % 2 %
Neo-Pentane 1.0000 % 2 %
i-Pentane 0.6653 % 2 %
n-Pentane 0.5513 % 2 %
Hexane 2.0854 % 2 %
Heptane 2.6785 % 2 %
CV 0.0276 % 0.1511 %
Table 1. Calibration gas accuracy effect towards CV calculation uncertainty
2. Calibration gas is as not as per the calibration gas certificate
On cold climate, this often happens on the heavy end components. Because the calibration
gas has been stored below its dew point temperature, the gas composition became non-
homogeneous. Some of the heavy end components condense and sit at the bottom of the
bottle. The calibration gas certificate is always used as the basis of the calibration gas
bottle concentration. However, when the gas is not homogeneous, it leads to an error. The
most common cases is illustrated in Figure 5 below.
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Figure 5. Non homogenous calibration gas
From the Figure 5, it can be seen that hexane and heptane response factor is lower than
expected. This is due to the gas being stored in the cold lower than its dew point
temperature. This issue if goes undetected can lead to quite significant mis-measurement.
However, this can be avoided by looking at the response factor trend as well as the
correlation chart. A healthy GC will have the property of RF trending and correlation as
shown in Figure 6.
Figure 6. RF trend and correlation chart of healthy GC
A healthy GC will have an ascending response factor trend and high correlation between
the Response Factor and Molecular Weight. The case where the heavy end sits at the
bottom of the bottle can be overcome by re-heating the gas to a homogenous state and
running the GC using calibration gas for several cycles. Test performed has shown that
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the detected gas return into its normal homogeneous state after 10 runs as shown in
Figure 7.
Figure 7. Runs of calibration gas prior to returning to homogenous state
Arguably after this process the composition within the bottle has been altered, however it
can also be argued that normally the heavy end has low concentration with low sensitivity
towards CV and density measurement and therefore the calibration gas will still be fit for
purpose. Also the acceptability of calibration gas can be determined by the gas thermal
conductivity property. Gas that flows through thermal conductivity detectors will follow
consistent characteristic as shown in Figure 6 earlier. As long as the RF trend is ascending
in the order of Methane – Nitrogen – CO2 – Ethane – Propane – iButane – nButane –
neoPentane – iPentane – nPentane – Hexane – Heptane, and the correlation between RF
and MW is high, it can be concluded that calibration gas is healthy as well as the valve and
other time events in the GC is healthy.
This principle can also be used to determine if a calibration gas is as per what stated in its
calibration certificate. There are some occasions where there have been errors in the
making of calibration gas which result in the bottle composition not as per the bottle’s
certificate. This can be determined by checking the calibration result.
The principal can also be used to identify human error in entering calibration data from
the certificate into the GC as shown in the case study below.
Case Study 1
The GC in this case study had been offline for a while, and it was time to bring it back
online again. A new calibration gas was installed and a calibration was done. Instead of
checking the trend and the result of the calibration, a forced calibration was performed
and GC was assumed to run correctly as it did not produce any alarm. However, because
it was a new calibration gas, the composition of the new calibration gas and the
composition of the old calibration gas that still existed in the GC were not the same. The
initial calibration RF trend on this GC is as the following:
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Technical Paper
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Figure 8. RF trend due to wrong component concentration entered in GC data table
Following this, component data table within the GC was changed to match the calibration
gas certificate and further calibration was performed. The result was a better response
factor, with several minor issues as shown in Figure 9.
Figure 9. RF trend after component data table in GC was adjusted
From Figure 9, the trend shows that N2 level was too high and hexane level was too low.
The N2 levels can be high after changing the calibration gas as the sample line can fill with
air. To rectify this issue, the calibration sample line was purged with calibration gas. After
clearing the air, the RF trend was significantly better as shown in Figure 10.
Figure 10. RF trend after calibration sample line has been purged
The blue line above shows the trend prior purging, and the red line shows the trend after
purging. The N2 is now at its expected level; however hexane RF was still lower than
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expected. Inspection of the correlation between MW and RF is then used to help determine
the cause of the low Hexane RF as shown in Figure 11.
Figure 11. MW-RF Log chart of calibration data
It was determined from the plot that based on the poor correlation of C1-C2-C6; the
problem was caused by some of the heavy component (hexane) leaving column 1 to flow
through column 2 instead of all of it being back-flushed due to incorrect valve timing. The
result was not all hexane component being detected by the GC and the RF reading low.
Adjustment was performed to the valve timing to prevent C6+ from entering column 2.
This resulted in the change of the response factor chart as depicted in Figure 12.
Figure 12. RF trend and MW-RF log chart of healthy GC
The charts now clearly indicate that the problem with the GC has been rectified and the
trends are all as expected. The error introduced by this problem may not be apparent at
the individual component level, however analysis of the resultant calculated calorific values
of the two calibrations clearly shows the difference to be significant. The potential
difference in the final output result is given in Table 2.
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Description Wrong RF Correct RF Difference
CV 45.07 44.44 1.41%
Volume 100 100
Volume 2,831,684 2,831,684
Energy (MJ) 127,624 125,840 1,784
Energy (KWh) 35,451,330 34,958,311 493,019
Value per KWh £0.02459 £0.02092
Value /day £871,748 £859,625 £12,123
Value /month £26,152,446 £25,788,746 £363,700
Table 2. Unhealthy vs healthy result comparison, Value per KWh data is taken from
Quarterly Energy Prices, December 2013
2.3 Repeatability Test
Repeatability test has been used a lot as part of GC preventive maintenance by many
operators. The tolerance used for repeatability test normally taken from ASTM
D1945:2001 [1], or GPA 2261:1995 [7] as shown in table 3 and 4 respectively.
Mole % Lookup Tolerance (absolute mole %)
0 to 0.1 mole% 0.01%
0.1 to 1 mole% 0.04%
1 to 5 mole% 0.07%
5 to 10 mole% 0.08%
Over 10 mole% 0.1%
Table 3. ASTM D1945:2001 section 10.1.1
Component Mole % Range Tolerance (percent relative)
Nitrogen 1 to 7.7 2
CO2 0.14 to 7.9 3
Methane 71.6 to 86.4 0.2
Ethane 4.9 to 9.7 1
Propane 2.3 to 4.3 1
Isobutene 0.26 to 1 2
n-Butane 0.6 to 1.9 2
Isopentane 0.12 to 0.45 3
n-Pentane 0.14 to 0.42 3
C6+ 0.1 to 0.35 10
Table 4. GPA 2261:1995 section 9
Although it has been used a lot, testing has been conducted to see the GC calculated CV
uncertainty if tolerance of ASTM D1945:2001 has been used. Dependent on the
composition, the CV uncertainty varies between 0.28% - 0.31%. This value is not
representative of the capability of modern GC where most of the modern GC is capable of
having CV uncertainty of below 0.12%.
Figure 13 below shows an example of 5 runs repeatability test performed on methane. It
can be seen from the illustration that the GC repeatability is far better than the set
tolerance.
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Technical Paper
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Figure 13. Five run repeatability test on methane
Furthermore, when a 40 hour repeatability test was done on methane, similar results were
seen: as demonstrated in Figure 14.
Figure 14. Forty hours repeatability test on methane
The result is also consistent to every other component of the gas, for example figure 15
shows the result for Propane.
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Figure 15. Forty hours repeatability test on propane
Based on these results, questions can be raised if this repeatability is really worth doing if
continuous monitoring is being performed. The cases where the repeatability test has
failed occur due to the following reasons:
1. Repeatability test was performed on un-normalised composition
2. GC calibration has already failed due to excessive response factor shifts
On another note, repeatability test can also lead to wrong impression. Passing repeatability
test does not mean that GC is accurate. It only means that the GC will provide answer
within a certain tolerance. The accuracy of the GC is not determined by repeatability test.
For example, GC can provide repeatedly wrong result when component data table is not
the same as actual value of the gas composition.
2.4 Control Chart
In many pipeline agreements, control charts have been stated as a requirement for
operators. The control chart is a plot of response factors and retention time of GC. The
issue with the control chart is that there are no standards to follow on what the control
limit to be used. Therefore, many versions of control limits in control charts have been
found. Some use 3 standard deviations of first 25 data, some other operators use 3
standard deviations of all data. However, none of these versions can determine how well
the GC has been working.
In fact control chart in the GC cannot be used in isolation because every component in the
GC is correlated. This means an error that occurs in one component will result in error of
every other components. This can be illustrated by the following example.
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Consider two control charts from GC A and GC B that have the same standard deviation
of three percent. Current practice says that both of this GC is performing equally good as
shown in Figure 16.
Figure 16. Control chart of methane RF on two different GC
The difference between these two GC is that on GC A, all components have the same exact
synchronous change of its response factors, while GC B has a completely random change
of its response factors. Figure 17 shows RF chart of two components (Methane and
Nitrogen) in the same chart.
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Figure 17. Methane and Nitrogen RF deviation trend
From Figure 17, it is visible that GC A chart is better than GC B chart. However, when GC
B chart is shown individually, it will only shows to individual components that both have
similar standard deviation as shown in Figure 18.
Figure 18. Methane and Nitrogen chart of GC B shown separately
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Looking at more components, it becomes very clear that GC A performs better than GC B
as shown in figure 19.
Figure 19. RF chart of 4 components for GC A and GC B
For the case of GC A, it will yield to 0% uncertainty regardless if the deviation is 3% or
10% or even 100% as when all the gas varies in the same exact way, it will always provide
the same normalised result. However, for the case of GC B where every gas response
factor behaves in random way, although each gas has similar standard deviation, GC B
has significantly higher uncertainty in comparison to GC A. The uncertainty comparison
between GC A and GC B is shown in Figure 20.
Figure 20. GC A vs GC B uncertainty
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This 3% standard deviation example is only meant to illustrate that GC A and GC B can
show the same deviation, but have completely different uncertainty outcomes based on
random vs synchronous variations in data. In fact this example cannot happen in an
actual GC because the measurement data gas to have a random spread, whereas GC A
data is derived from simulated absolute numbers that move synchronously. This
example shows that looking at individual component control charts alone cannot be used
to confirm the health of a GC. It is only when every gas component is analysed and
plotted together and there individual and collective uncertainty values calculated will one
get a proper representation of actual GC performance
Figure 21 shows a control chart for methane of a healthy GC. From the Figure 21 below,
it looks like the methane has gone out with the 2 std deviation limit and therefore based
on the current practice, GC may have been performing out with its acceptable limit.
Figure 21. Methane control chart of a healthy GC
However, when the full RF chart is drawn in the same chart as shown in Figure 22, it can
be seen that GC has been performing well. From the chart it can be seen that all
components varies in similar general trend. Also from the chart, it is visible that hexane
and heptane response factor has more variation in comparison to the rest of the
components.
Figure 22. Healthy GC RF chart
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When the chart is interpreted in terms of uncertainty value of each gas, it can be seen
that hexane and heptane has higher uncertainty value in comparison to the rest of the
component. It can also be seen the uncertainty toward CV measurement is very low, much
lower than the normally assumed CV uncertainty of between 0.2% - 0.3%.
The monitoring of uncertainty trend can be used to monitor longer term GC performance
including early failure detection. Alarm limit can be placed towards the uncertainty value
and at any point in time GC performance can then quantified in terms of its uncertainty
value as shown in Figure 23.
Figure 23. Uncertainty trend of GC derived from RF data
2.5 Composition Comparison
In many facilities, redundant GC is implemented as a fail save feature of measurement.
However, the redundant GC is also often used as a validation tool of each GC
measurement. However, in many places the component comparison is performed on un-
normalised basis. And because of this, many times the GC failed to perform within its limit
due to the wrong procedure of comparison.
Consider another GC A and GC B measures the same gas, and both of the GC are
configured to measure an un-normalised composition. The measurement result is shown
in Table 5.
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Description GC A GC B Difference Tolerance Status
Methane 86.7944 83.3907 3.4037 0.1 Fail
Nitrogen 5.6327 5.4118 0.2209 0.08 Fail
CO2 2.0359 1.9560 0.0798 0.07 Fail
Ethane 4.3703 4.1989 0.1714 0.07 Fail
Propane 1.8412 1.7690 0.0722 0.07 Fail
i-Butane 0.2548 0.2448 0.0100 0.04 Pass
n-Butane 0.3546 0.3407 0.0139 0.04 Pass
Neopentane 0.1018 0.0978 0.0040 0.01 Pass
i-Pentane 0.3068 0.2948 0.0120 0.04 Pass
n-Pentane 0.2041 0.1961 0.0080 0.04 Pass
Hexane 0.1033 0.0993 0.0041 0.04 Pass
Total 102 98
Table 5. Un-normalised result comparison between GC A and GC B
As shown on Table 5, the result has failed. However when the result is normalised, both
GC shows the same exact result as shown in Table 6.
Description GC A GC B Difference Tolerance Status
Methane 85.09254 85.09254 0.0000 0.1 Pass
Nitrogen 5.522274 5.522274 0.0000 0.08 Pass
CO2 1.995952 1.995952 0.0000 0.07 Pass
Ethane 4.284621 4.284621 0.0000 0.07 Pass
Propane 1.805088 1.805088 0.0000 0.07 Pass
i-Butane 0.249819 0.249819 0.0000 0.04 Pass
n-Butane 0.347691 0.347691 0.0000 0.04 Pass
Neopentane 0.099842 0.099842 0.0000 0.01 Pass
i-Pentane 0.300822 0.300822 0.0000 0.04 Pass
n-Pentane 0.200065 0.200065 0.0000 0.04 Pass
Hexane 0.10129 0.10129 0.0000 0.04 Pass
Total 100 100
Table 6. Normalised result comparison between GC A and GC B
This example shows that when performing comparison between two or more GC, the
comparison has to be made in normalised value.
2.6 ISO 10723 Multilevel Calibration
ISO 10723:2002 standard [3] was developed to quantify GC repeatability and linearity. It
also provides a method to correct for the non-linearity of thermal conductivity detector in
case GC needs to measure large variation of gas. This case may happen if the GC measures
gases that come from different sources, such as different wells, export composition that
may differ from import composition, etc.
In the recent years it has gained popularity in Europe as part of the Commission of the
European Communities decision [4] that enforce all GC which is used to measure gas
emission to be validated using ISO 10723:1995 [8] as a performance benchmark on yearly
basis. Although the method is very good to determine and correct for non-linearity in GC
detectors, recent study shows that it does not require to be performed on a yearly basis.
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Also, the latest Commission Regulation (EU) No 601/2012 [5] has omitted the requirement
for ISO 10723 and only requires routine validation of the GC with no specific preference
of the validation method.
The following are few case studies from the current practices of ISO 10723 performance
test.
1. Two tracking GC where one failed ISO 10723 performance test
This case study shows where GC A and GC B have been tracking each other very well.
However when ISO 10723 performance evaluation test was done on both of the GC’s, GC
A failed the test while GC B passed. After investigation it was found that the test failed in
the composition area where the GC has not been operating as can be illustrated in Figure
24.
Figure 24. ISO 10723 test range on methane
From Figure 24, it is illustrated that throughout the year the range of methane going
through the pipeline is between 82 – 86%. ISO 10723:2002 [3] specifies that the GC to
be tested with 7 different gases with the range as shown in Figure 25.
Figure 25. Test gas mixture range for ISO 10723 performance test
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Following the formula, for the gas range illustrated in Figure 24, the methane gas
concentration range should lie between 81 to 87 mole%. However, the test gas range on
this case was between 78 to 98 mole%. Most of the tested range will never be measured
by the GC as historically GC only has range between 82 – 86 mole%.
Having a broader range may appear to be a good thing to do, however looking at the failed
result of the non-operating region, it would be fairer to perform the test over the actual
gas range being measured since the non-linearity picked up on GC A had not affected its
accuracy of measurement.
2. GC is proven to be linear for its operating range
In some cases, ISO 10723 is performed regardless if there is actual need for it. One can
argue that if the GC composition always fall within the linear range of the detector, then
ISO 10723 is not necessary.
The difference between multilevel calibration constant implemented mole % and single
point mole % is that the multilevel calibration corrects for the non-linearity of detector
using a polynomial curve. Single point calibration mole % assumes that detector is fully
linear. The calculation of single point calibration mole % is shown in Equation 1.
𝑥𝑖 =𝑃𝑒𝑎𝑘 𝐴𝑟𝑒𝑎
𝑅𝑒𝑠𝑝𝑜𝑛𝑠𝑒 𝐹𝑎𝑐𝑡𝑜𝑟
Where: 𝑥𝑖 = mole % of component i
Equation 1. Single point mole % calculation
Multilevel calibration mole % calculation is shown in equation 2.
𝑥𝑖 = 𝑏0 + 𝑏1𝑦𝑖 + 𝑏2𝑦𝑖2 + 𝑏3𝑦𝑖
3
Where: 𝑥𝑖 = mole % of component i
𝑏𝑛 (n = 1, 2, 3, 4) parameters of analysis function
𝑦𝑖 = peak area of component i
Equation 2. Multilevel calibration mole% calculation
Figure 26 and Figure 27 shows a comparison between mole% of methane produced by
multi-level calibration constant (MLC) implemented vs single point calibration constant
implemented.
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Figure 26. Methane MLC implemented mole % vs single point implemented mole %
Figure 27. Difference and tolerance between MLC and single point implemented mole%
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From Figure 26, it can be seen that the difference is negligible and well within the tolerance
specified by ISO 10723:2002 [3] as shown in Figure 27.
When the gas always falls within the linear range of the GC such as the example above,
the ISO 10723 performance test should not be required. Therefore the method is more
suitable for laboratory GC due to the wider range of composition it would be exposed to
that to an online metering GC that measures stable composition with little variations.
3 Conditional Based Monitoring
In recent years, method for GC conditional based monitoring has been developed that
allows constant monitoring of GC parameters. This method has proven to provide
confidence of the GC throughout the year by simply monitoring a few parameters of the
GC detailed as follows:
3.1 Response factor trend and correlation chart
Response factor trend and correlation chart are two very valuable tool to determine that
GC is healthy in terms of all its time events settings, and that the calibration gas
concentration is as per stated in its calibration certificate. The RF trend and correlation
chart is shown in Figure 28.
Figure 28. Response factor trend and correlation chart
The RF trend needs to be ascending. When a composition on the right hand side is lower
than the left hand side, it is an indication that something is not right with the GC. For
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instance Figure 29 shows that the gas is not purged enough due to high level of Nitrogen;
also there is valve timing issue due to low level of hexane response factor.
Figure 29. Response Factor of un-healthy GC
When such issue exist in the GC, correlation chart will also show a bad result. Figure 30
shows correlation chart associated with the same data as shown in Figure 29.
Figure 30. Correlation chart of un-healthy GC
The method can then be used to ensure that the GC is healthy at any point of time prior
to monitoring the longer term health of the GC. Because of the repeatable nature of a GC,
it operates in a repeatable manner with consistent a systematic error. Therefore it is
important to ensure that both GC is measuring accurately and calibration gas
concentration is as per the calibration gas certificate.
3.2 GC uncertainty monitoring
As described in section 2.4, the uncertainty of GC parameter is one of the ways to quantify
GC performance derived from response factor control charts. The monitoring of the GC
response factor not only will ensure the health of the GC throughout the year, but also will
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provide with early indication in case of deterioration of GC performance as it will be
revealed by increment of the GC uncertainty value.
Healthy GC response factor trend is shown in Figure 31.
Figure 31. 1 year RF trend of healthy GC
Visually from the trend, many stories can be told. From Figure 31 it can be seen that there
was a shutdown between August 2013 and October 2013. There was also change in
calibration gas in April 2015 and some parameter changes were done on GC in June 2014.
Also it can be seen visually that all response factor trends up and down in harmonious
way. Uncertainty trend is one way to quantify these parameters. Uncertainty trend of the
GC associated with Figure 31 is shown in Figure 32.
Figure 32. Uncertainty of CV associated with Figure 31
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From here uncertainty limits can be set and alarm flagged at any time the uncertainty
value exceed the limit. Figure 32 shows an example where uncertainty limit is set to
0.12%. This limit is very useful to catch issues with GC before the issue becomes
significant.
Figure 33. Uncertainty with set limit of 0.12%
3.3 Calibration data update monitoring
To get the best result, automatic calibration on the GC should be active. GC can be
automatically calibrated every day or every two days. When calibration data is not updated
in a GC, it is an indication that calibration has failed. The monitoring of this calibration
updated on online conditional based monitoring system shows that one of the following
has occurred:
Communication failure between GC and CBM system
Calibration failure has occurred
Both occasions can easily be checked. The three parameters (R2, Uncertainty, and
calibration data update) when checked continuously will provide continuous confidence on
the GC measurement. A dashboard system can also be provided to show these three
parameters for daily check as shown in Figure 34.
Figure 34. Dashboard to of GC health status
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It has also been learned that with the increased GC confidence, the GC that is historically
blamed for many issues with the process has now become the source of confidence of
measurement which can be used to validate other systems such as pressure let down
system that feed the gas to the GC.
3.4 Pressure let down system validation
With the increase of the confidence in GC measurement, when the GC result is compared
against spot sampling, it will provide the following information:
If the sample collected is representative
If sample let down system provides the GC with representative sample
It is possible to see if the sample collected is representative of what the pipeline
composition is by looking at Nitrogen value as well as the methane value. These two
components are very light and have very low dew point temperature, therefore it is
expected that these two components will be comparable to the GC component. Figure 35
shows a case where three samples have been taken.
Figure 35. Nitrogen GC result vs spot sample
The first sample shows that there is air contamination during the spot sampling process.
It shows high level of Nitrogen in comparison to the GC reading. The other two sampling
show better correlation between spot sample result and GC result. Both of these results
fall within acceptable reproducibility limits as stated in ASTM D1945 standard. A similar
result is shown in methane component as shown in Figure 36.
Figure 36. Methane GC result vs spot sample
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When all the components are checked, heavy end drop out can also be detected as shown
in Figure 37.
Figure 37. Heavy end detection
Undetected heavy end drop out has proven to be a big issue. From case studies, errors of
more than £100,000.00 /month have been detected using this method.
3.5 Auditable comment
One of the most useful features of the conditional based monitoring tool is the auditable
comment. Any events that happen in the GC can have an associated comment. This makes
analysis of historical data easy for anybody that has interest in the particular GC
maintenance. A comment system can be made where every comments is linked to a
particular events such as shown in Figure 38.
Figure 38. CBM comment feature
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Each event that has been done in the GC can then be traced and analysed from cause and
effect perspective.
3.6 Conditional based monitoring overall impact
In effect the overall impact of conditional based monitoring tools is to virtually eliminate
the need of conventional maintenance of the GC. The maintenance requirement that can
be handled by conditional based monitoring is summarised in Table 7.
Description Remarks
Daily health check / validation Correlation and uncertainty feature
Early failure detection Uncertainty feature
Valve timing check Correlation feature
Calibration gas correctness check Correlation feature
Pressure let down validation Trending comparison between GC and spot sample
GC uncertainty check On daily basis
Confidence in GC On daily basis
Table 7. GC conditional based monitoring functions
4 Conclusion
This paper has shown the conventional GC maintenance methods that have been used in
the industry and also a new novel method that may increase the confidence in the GC
operation while eliminating the need for conventional maintenance methods (i.e.
continuous performance monitoring). The conclusion that can be taken is that the
conventional maintenance method although is widely used by the industry, it adds little
value towards overall GC confidence. GC still fails with the need of specialist knowledge to
rectify the situation, but not having enough detailed background information to analyse
the actual cause of the failure.
The idea of conditional based monitoring provides operators with full confidence of the GC.
Although some errors in GC’ may still require specialist knowledge to rectify, the source
of the issue can be traced by looking at complete historical events that’s recorded in a
database.
The implementation of the conditional based monitoring is easy without the need for
change of any equipment currently being used.
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5 References
[1] ASTM D1945. Standard test method for analysis of natural gas by gas
chromatography. ASTM, 2001.
[2] BS EN ISO 10715. Natural gas - sampling guidelines. BS EN ISO, 2001.
[3] BS EN ISO 10723. Natural gas - performance evaluation for on-line analytical
systems. BS EN ISO, 2002.
[4] Commission Decision 2007 589 EC. Commission Decision. Establishing guidelines
for the monitoring and reporting of greenhouse gas emissions pursuant to Directive
2003/87/EC of the European Parliament and of the Council. Official Journal of the European
Union, May 2007.
[5] COMMISSION REGULATION (EU) No 601/2012. The monitoring and reporting of
greenhouse gas emissions pursuant to Directive 2003/87/EC of the European Parliament
and of the Council. Official Journal of the European Union, 2012.
[6] Encyclopaedia Britannica. Joule-Thomson effect. britannica.com. Accessed January
13, 2015. http://www.britannica.com/EBchecked/topic/306635/Joule-Thomson-effect.,
2015.
[7] GPA 2261. Analysis for Natural Gas and Similar Gaseous Mixtures by Gas
Chromatography. GPA, 1995.
[8] ISO 10723. Natural gas - performance evaluation for on-line analytical systems.
ISO, 1995.