A Comprehensive Cost-effective Dissolved Gas Monitoring Strategy

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    A comprehensive, cost-effective dissolved gas monitoring strategy

    Stephan Brauer Trevor Lord

    Morgan Schaffer Inc. Lord Consulting

    EEA Conference & Exposition 2012, 20-22 June, Auckland

    ABSTRACT

    This paper reviews an innovative, cost-effective approach for deploying on-line dissolved gas

    monitors on a population of liquid-filled transformers to achieve both comprehensive fault

    detection and well-informed maintenance decisions when a fault is detected. Under this

    approach, fault-detection monitors are installed on the majority of units, with alarm limits

    optimized for each unit based on historical dissolved-gas levels. The fault-detection monitors

    are designed and installed in such a manner that if an anomalous gassing condition is

    detected, the fault-detection monitor can be readily interchanged with a multi-gas monitor to follow the fault evolution in real-time using complete dissolved gas analysis. New

    measurement technology also allows this concept to be applied to tap changers using the

    latest Duval Triangle for LTC units. The approach is a natural complement to routine oil

    sampling and laboratory analysis, as part of a comprehensive transformer asset management

    program. Requirements for accuracy, reliability and measurement ranges are reviewed. Field

    experience with suitable monitors is presented using illustrative case studies.

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    INTRODUCTION

    Dissolved gas analysis (DGA) is widely accepted to be one of the most effective tools

    available for assessing the operational health of large, liquid-filled transformers [1,2]. With a

    history of more than 40 years of oil-syringe sampling and laboratory measurements, DGA

    methods continue to evolve as new technology solutions emerge. Increasingly, DGA

    measurements are being conducted within the transformer yard, using portable analysers and

    on-line monitors. On-line DGA has come to play a central role in optimizing operations and

    asset management [3] within the electrical power industry.

    Historically, two categories of on-line dissolved gas monitors have been established. The first

    are fault-detection monitors designed to sense primarily hydrogen as the key gas associated

    with all transformer fault modes resulting in oil-degradation. These monitors may also

    measure dissolved carbon monoxide associated primarily with the degradation of cellulose

    insulation [2]. In the second category are multi-gas monitors that measure most or all of the gases of a typical DGA laboratory. The emergence of monitors that measure 3-5 gases has

    since blurred this distinction, offering new price/performance combinations to the industry.

    Also, considerable progress has been made in improving the accuracy and reliability available

    from on-line dissolved gas monitors. Dissolved moisture measurement has become a standard

    feature of most DGA monitors.

    In this paper, we focus on an approach to DGA monitoring that seeks to provide asset

    managers with the greatest ability to detect and diagnose transformer faults across a

    transformer population, for a given total cost of monitor ownership. Under this approach, we

    use the historical categorization mentioned above. Fault-detection monitors are installed on

    many units, in a manner that offers the highest assurance of fault detection with a minimum

    of false alarms and monitor service events. Each fault-detection monitor is designed and

    installed in such a fashion that if an anomalous gassing condition is detected, it can be readily

    interchanged with a multi-gas monitor. The latter allows the fault evolution to be studied in

    detail using complete dissolved gas analysis, such that well informed decisions can be taken

    to manage the fault condition. Design and installation features that facilitate the interchange

    of monitors are described. Also, performance requirements and cost of ownership are

    discussed for DGA monitors that best serve this monitoring model.

    ON-LINE DISSOLVED GAS MONITORING

    The fundamental requirement of a fault-detection monitor is the ability to unambiguously

    report an alarm condition when a key gas, normally hydrogen, has reached an anomalous

    level. To accomplish this assuredly and without false alarms, the monitor must be built

    around a dissolved-gas-measurement system that is stable and dependable over many years of

    field service. Monitors that deliver accurate dissolved gas concentrations are preferred for

    several reasons. First, a measurement system which is consistently accurate, as benchmarked

    to a qualified DGA laboratory, generally meets the requirement for good stability. Also,

    absolute accuracy implies good gas-selectivity, so that changing levels of potential

    interference gases do not compromise the key gas reading. Accurate and selective fault-

    detection monitors offer the additional advantage that historical laboratory DGA data from

    each specific transformer (or factory acceptance data in the case of new transformers) can be

    used to set optimal and justifiable gas alarm thresholds to protect each unit. This key step in

    the commissioning of a monitor is often completed using excessively wide margins, or using

    values drawn from published standards which may not be optimal for the unit. Accurate

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    monitors allow transformer asset managers to establish consistent policies for setting alarm

    levels based on well-established DGA baselines, and to have these policies endorsed by their

    management and insurance companies. Finally, accurate and selective monitors allow

    comparison with routine annual laboratory DGA results, in order to validate the performance

    of the monitor periodically throughout its working lifetime. Independent studies of monitor

    accuracy are ongoing [4].

    Reliability and accuracy are also paramount requirements for a multi-gas monitor, whether

    permanently installed on a critical transformer, or used within the monitoring model

    prescribed here. The complex process of diagnosing a fault condition on an in-service

    transformer benefits from certainty in the dissolved gas-concentrations. As a guide to the

    accuracy requirements of the monitor, it is noted that the various DGA condition assessment

    tools known in the industry were developed using laboratory DGA measurements, and the

    expectations of accuracy from a good DGA laboratory are documented [5].

    Several factors suggest that some online multi-gas monitors have the potential to actually be

    more accurate than DGA labs. Good monitors control the oil temperature during the gas-

    extraction process, so the gas-solubility temperature dependence does not impact the

    readings. Also, monitors that use a continuous oil-flow circuit are largely free of poor oil-

    sampling techniques, oil-sample storage issues, and syringe gas-bubbles, which can be

    dominant limitations to the accuracy of DGA results obtained from even the best of

    laboratories. Monitors also offer favourable measurement statistics, since many readings can

    be easily averaged to reduce random measurement errors. Finally, as shown in the case

    studies below, operating transformers are seldom in a steady -state. Improved agreement with

    lab samples can be obtained if the sampling location is on the DGA monitor, and the time of

    the sample collection is recorded for comparison with the monitor readings from the same

    time.

    In comparing monitor and laboratory DGA measurements, it is helpful to consider the gas

    extraction techniques used by each. Techniques with extraction efficiency near 100%,

    including as ASTM-D3612 Method A and others [6], are fundamentally insensitive to the gas

    solubilities, which are known to vary with fluid type, age, contamination, and even the nature

    of the gas matrix [7, 8]. However, most labs today use more solubility-sensitive headspace

    extraction techniques because they are more cost effective. Since the actual solubility of a

    syringe sample is not generally known, many of these labs report dissolved gas readings

    based on Ostwald solubility coefficients for mineral oil published in ASTM-D3612 [9]. If the

    fluid is not mineral oil, or is aged, contaminated, or saturated with gas, the reported dissolved

    gas concentrations would not be expected to agree with those measured by high-efficiency

    extraction methods. Multi-gas monitors commonly use a headspace extraction technique, and

    are thus subject to the same concern. Therefore, when configuring a multi-gas monitor, the

    accuracy objectives should be considered. For absolute accuracy and comparison with high-

    efficiency extraction methods, monitors should be configured with the Ostwald solubility

    settings for the actual liquid in the transformer. On the other hand, if the objective is to have

    the monitor report readings which are as similar as possible to a lab using headspace

    extraction, it may be best to configure the monitor with the solubilities from ASTM-D3612.

    (As for moisture-in-oil, monitors measure %RS in the oil and may convert this to water

    content (in ppm) using a solubility function. For best agreement with laboratory Karl Fischer

    water content, the moisture solubility coefficients for the actual liquid should be configured

    in the monitor.)

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    As far as we are aware, little work has been conducted to explore fault diagnostic techniques

    at sub-ppm gas levels, primarily because such measurements have not historically been

    available. Although industry standards suggest that 2 ppm of C2H2 can be reason for concern

    in some transformers, many labs have a detection limit of 2 ppm for routine DGA analysis.

    Some multi-gas monitors have detection limits of 0.2 ppm for C2H2 and other gases, offering

    the potential to reveal fault behaviour at earlier stages than had previously been possible.

    Utilities have been conducting laboratory DGA measurements for load-tap- changer (LTC)

    transformers for many years, and improved methods for interpreting LTC faults from DGA

    data have received considerable recent attention [10, 11]. We believe the monitoring model

    proposed here may help extend the advantages of on-line DGA monitoring to this class of

    fault-prone transformers. Dissolved fault-gas concentrations from LTC units can exceed

    100,000 ppm in extreme cases [11], so monitors with high measurement top-of-range (TOR)

    are warranted, both for fault-detection and for multi-gas DGA monitoring.

    COST CONSIDERATIONS

    Cost-benefit analysis for on-line transformer monitoring, in the broadest sense, has been

    described in some detail [3]. Such models make a compelling case for on-line monitoring, the

    main economic advantages arising from reduced catastrophic failures, reduced interruptions

    to power generation and delivery, transformer lifetime extension, and potential gains from

    sustained overloading. One conclusion is that there is economic benefit for on-line

    monitoring, including on-line DGA monitoring, on most every transformer above a certain

    replacement cost, the threshold being determined by the cost of the monitoring equipment. To

    experience these benefits across the greatest portion of a transformer fleet, an economic DGA

    monitoring solution is desirable, particularly for lower MVA asset classes. The same position

    can be reached directly from the annual capital or operating budget of any transformer asset

    manager. The monitoring approach offered here provides a practical solution to maximizing

    asset protection within budgetary constraints.

    Table 1: Two DGA monitoring scenarios for a population of 10 transformers.

    Assumptions Fault detector Multi-gas

    Purchase price 10,000 $ 35,000 $ Relative dollars units,

    Consumables at installation 1,000 $ where the cost of a

    Installation labour and materials 1,000 $ 1,250 $ fault detection

    Acquisition cost 11,000 $ 37,250 $ monitor is $10,000

    Routine annual inspection 500 $ 500 $

    Routine annual consumables 1,000 $

    Annual cost of false alarms 100 $ 100 $

    Allocation for repairs 100 $ 500 $

    Annual operating cost 700 $ 2,100 $

    Scenarios Lifetime costs

    Lifetime (years) 15 Acquisition Operating Total

    Multigas only (monitors) 10 372,500 $ 315,000 $ 687,500 $

    Fault-detect & Multi-gas (monitors) 10 1 147,250 $ 136,500 $ 283,750 $

    Difference 225,250 $ 178,500 $ 403,750 $

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    Table 1 presents two simple DGA monitoring scenarios with similar levels of transformer

    protection for a population of 10 transformers. We have chosen to use relative dollar units,

    where the cost of a fault-detection DGA monitor meeting the criteria described above is

    $10,000. The more complex measurement systems within multi-gas DGA monitors make

    them typically 3-4 times more costly to purchase. The costs of operating online monitors

    include annual inspections, routine maintenance, repairs, and, in the case of multi-gas

    monitors that satisfy assumptions above, the cost of replacing consumables. (We have

    assumed an average cost per year although the replacement interval for consumables is two

    years on some multi-gas monitors.) The cost of addressing false alarms has been assumed

    small due to the choice of accurate and reliable monitors. This simple model reveals the main

    cost advantages of the proposed monitoring approach. For the same level of transformer

    protection, monitor acquisition costs and lifetime ownership costs are much reduced.

    INTERCHANGABLE MONITORS

    Calisto products [12] are designed to facilitate the interchange of fault detection and multi-

    gas monitors. Most importantly, these monitors meet the performance requirements outlined

    above. Common operating features that facilitate comparison of the DGA results between

    these monitors include 1) an oil circulating pump, 2) temperature conditioning of the oil at

    the extraction stage and the gas measurement system, 3) the same user-interface software

    with local or network database, 4) a front-panel display with 3-button navigation, and 5) an

    oil-sampling port to allow oil-syringe samples to be drawn for comparison with DGA lab

    measurements.

    With appropriate planning of the installation site, the process of interchanging a fault-

    detection model with a multi-gas model is straightforward, and can be performed without

    taking the transformer out of service. As shown in Figure 1, both monitor types have similar

    physical dimensions and share common mounting-hole patterns and shock-mounts. The oil

    inlet and outlet ports have the same fittings and similar locations, being only 11 cm (4.5

    inches) further apart on the multi-gas models. Internal to these units are oil valves that

    minimize oil spillage during a swap. Optional external oil valves can also be installed near

    the connections to the unit to similarly limit oil spills from the oil lines when a unit is

    disconnected. We have conducted laboratory measurements to quantify the reaction of C2H2

    dissolved in mineral oil with 3/8 copper tubing at elevated oil temperatures. Our measurements indicate that the reaction is sufficiently slow as to be negligible with the oil-

    flow rates typical of these monitors. It is nevertheless recommended to use stainless steel oil

    lines of solid tubing, braided hose, or a combination of these, to alleviate any doubt about

    possible reaction of C2H2 in copper lines.

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    Figure 1: Installation of interchangable fault-detection (left) and multi-gas DGA monitors

    (right).

    The electrical connections to these monitors have also been designed to anticipate the

    interchange of different models. A removable plate on the bottom of the enclosure can be

    modified to suit the users preferred conduit termination, and this plate is identical on all

    models, minimizing the re-work required to make water-tight electrical feed-throughs when

    units are interchanged. The models also use the same electrical connectors and terminal strips

    for digital communications, analogue inputs/outputs, and relay outputs.

    FIELD STUDIES

    Figure 2 shows data recorded by a fault-detection monitor installed on a 700 MVA free-

    breathing autotransformer located in Norway. The unit has been running with the same

    mineral oil since 1978, which has been regenerated once. The H2 level 1 alarm was set to 50

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    ppm, and the CO level 1 alarm at 1000 ppm. The case is uncommon in that a CO alarm was

    reported (on 12/07/2011), and only subsequently were smaller increases in H2 and WC

    discovered. The manufacturer indicated that this transformer design includes sections of thin

    copper foil covered with paper for electrostatic screening of the outer legs. Repairs on similar

    units have shown that eddy-current heating of the foil can create localized hot regions which

    may burn the paper creating CO and CO2, and generate small amounts of other fault gases. The unit remains in service with close attention to the DGA monitor readings and alarms.

    Figure 2: Development of a fault involving both oil and celulose insulation, recorded by a

    fault-detection monitor.

    When catastrophic failures occur on monitored transformers, post-mortem analysis often

    shows that a rising H2 signature was recorded. For most of these failures there is adequate

    time for intervention, but the H2 rise is not followed by operator action because the alarm

    thresholds were not optimally set, or the alarm is considered erroneous. An example is

    depicted in Figure 3 where, in early summer, a gassing fault accelerated with the increase in

    peak daily load, but was not detected because the H2 alarm thresholds were not optimized

    based on the low historic H2 level.

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    Figure 3: Development of a catastrophic fault involving both oil and celulose insulation,

    recorded by a fault-detection monitor.

    When a fault-detection monitor is installed, mechanical, plumbing and electrical provisions

    can be prepared to allow a multi-gas monitor to be installed in parallel, should it become

    necessary. An example of such an installation is presented in Figure 4, which shows a fault-

    detection monitor (left) and full DGA multi-gas monitor (right), installed on the same

    transformer.

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    Figure 4: Fault-detection and multi-gas monitors installed in Malaysia with stainless-steel

    oil lines and custom-made sun shields.

    Figure 5: On-line DGA data showing moisture and gassing behaviour that varies with load.

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    Figure 5 presents data from a multi-gas monitor on a 20 MVA free-breathing transformer

    filled with mineral oil, which was put into service in the USA in 1969. The monitor reported

    a high average moisture level near 33 ppm water content (WC) or 49 %RS@25C. Daily

    transformer load cycles generated daily cycles in WC of about 2-4 ppm peak-to-peak as

    moisture was driven out of the cellulose insulation and into the oil with higher core

    temperature. The data also shows small daily variations of fault-gases (2-3% peak-to-peak)

    which correlate to the moisture. Note that sub-ppm changes were resolved for C2H4 and CH4.

    Duval triangle analysis using the average values of CH4, C2H2 and C2H4 indicates a D1 fault

    type (low energy discharges). The observation that each of these three gases rose and fell in

    unison suggests that the D1 fault was load-dependent, a plausible behaviour. The same

    pattern is discernible in the H2 data, but none of the other gas readings, adding weight to this

    interpretation. The small slow downward trend of fault gases may have been related to

    seasonal changes in load and ambient temperature in this late-summer data. Historic

    laboratory DGA data were in agreement with the monitor data. This example shows how

    time-resolved DGA measurements can offer insight into the complex dynamic behaviour of

    an energized transformer.

    Figure 6: Multi-gas DGA monitoring of a defective new transformer.

    Figure 6 is data taken within the first days of service of a new 900 MVA transformer filled

    with mineral oil, installed in the USA. A multi-gas monitor was installed on the unit and put

    into service before the transformer was energized on 14/10/2011. Within a few hours of

    operation, the transformer began to exhibit significant fault gassing. The monitor readings

    rose steadily over 24 hours, and the transformer was de-energized late on 15/10/2011, after

    which the gas levels quickly stabilized. Laboratory DGA samples confirmed the

    concentrations reported by the monitor. Duval triangle analysis suggests a T3 fault (thermal

    fault > 700C), which could have quickly escalated to a catastrophic failure. The

    comparatively-constant CO readings suggest the cellulose insulation was not directly

    involved. The transformer was returned to the manufacturer for root cause analysis and repair

    under warranty.

    CONCLUSIONS

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    Accurate multi-gas online DGA monitors can provide valuable insight into the complex

    dynamics of gassing behavior associated with transformer faults. The advantages of such

    tools can be extended across a population of transformers economically through the strategic

    deployment of interchangeable fault-detection detectors of high accuracy and reliability.

    REFERENCES

    1. IEEE Guide for the Interpretation of Gasses Generated in Oil-Immersed Transformers, IEEE Standard C57.104-1991, 1991.

    2. Mineral oil-impregnated electrical equipment in service Guide to the interpretation of dissolved and free gases analysis, IEC Publication 60599, 1999.

    3. IEEE Draft Guide for Application of Monitoring Liquid-Immersed Transformers and Components, IEEE Draft Standard C57.143-2006.

    4. Report from CIGRE WG47, in development. 5. M. Duval, J. Dukarm, Improving the Reliability of Transformer Gas-in-Oil

    Analysis, IEEE Electrical Insulation Magazine, vol. 21, no. 4, pp. 21-27, 2005. 6. M. Duval, New Techniques for Dissolved Gas-in-Oil Analysis, IEEE Electrical

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    7. M. Cyr, Determination of Ostwald solubility coefficients in modern transformer oils, Minutes of PdM SA Conference, Johannesburg, 2010.

    8. J. Jalbert, R. Gilbert, P. Ttreault, and M. A. El Khakani, Matrix Effects Affecting the Indirect Calibration of the Static Headspace-Gas Chromatographic Method Used

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    9. ASTM Standard Test Method for Analysis of Gases Dissolved in Electrical Insulating Oil by Gas Chromatography, ASTM Standard D3612-02, 2002.

    10. M. Duval, The Duval Triangle for Load Tap Changers, Non-Mineral Oils and Low Temperature Faults in Transformers, IEEE Electrical Insulation Magazine, vol. 24, no. 6, pp. 22-29, 2008.

    11. IEEE Guide for Dissolved Gas Analysis in Load Tap Changers, IEEE Standard C57.139-2010

    12. Morgan Schaffer Inc., 8300 St-Patrick Street, Suite 150, LaSalle, Qubec, Canada.