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Transformer oil analysis methods

transformer-oil-regeneration-by-Globecore

Transformer oil and solid insulation are subject to natural wear and aging in the process of transformer operation. Therefore, it is imperative that periodic samples be taken for analysis and timely improvement of oil quality, before bad quality oil can cause degradation of insulation.

The rate of natural aging and wear degrading insulation materials performance, depends on several factors, such as oil type, system tightness (air tightness), operating temperature, content of water in insulation, as well as amount and type of contamination.

Since most transformers in the United States are sealed and do not allow air or water inside, degradation of oil performance may be very slow over many years. Therefore, the oil in many American transformers which have been operated for over 30 years is still in good condition.

Schedule of sampling varies depending on type of analysis, significance of equipment, availability of information on malfunction or problem and whether this type of transformer has had certain problems before.

Most of the tests done in North America are based on ASTM methods. In Europe and other countries worldwide, such tests are run according to IEC TC10.

Analysis of insulation liquid requires an array of physical and chemical test parameters.

There are many other tests, but the above are the most important and should be scheduled regularly. The above test allow to assess oil quality, but they do not provide in-depth diagnosis based on operation conditions or equipment health.

Physical tests include interfacial tension, settling temperature, viscosity, color etc. Parameters like water content, acidity, oxidation of inhibitor and PCB content are analyzed chemically. Electric tests include dielectric breakdown voltage test and power factor.

There is, however, a method used for analysis of transformer oil, which helps to diagnose electric equipment condition. This is the DGA gas chromatography test.

Gas chromatography has been used for analysis of gases in petroleum products for decades, although the dissolved gas analysis had not been used for transformer oils until 1970s.

Early on, this method was promoted by Dr. James Morgan of Morgan Schaffer Systems, Canada, and researchers J.E. Dind, R. Daust and J. Regis of Canadian utility Hydro-Quebec. Since the method proved very efficient and provided ample diagnostic information to detect impending malfunctions, it was soon adopted by other labs as well, including Doble Engineering in Massachusetts.

The DGA is now a standard in service industry worldwide, and is thought to be the most important test of insulation liquids in electrical equipment.

Indeed, the ability to detect such a wide range of problems makes this method a powerful tool for both detecting impending malfunctions and determining the cause of such malfunctions.

This test, performed in accordance to ASTM D3612 or IEC 60567, is, at present, the most needed and the most important diagnostic of transformer oil, as insulation degrades from overheating or overloads. Gas is a byproduct of this degradation and can be analyzed to determine the causes and conditions of the malfunction.

Dissolved gases can be detected in low concentrations (at ppm level), which allow timely intervention before electric equipment fails, including repairs during scheduled maintenance.

The DGA method involves extraction or absorption of gases from the oil and injection of these gases into gas chromatographer (GC).

To determine gas concentration, flame ionization detector (FID) and thermal conductivity detector (TCD). Most of these systems also use methanizer, which transforms any carbon oxide or dioxide into methane and then detects the gas by a very sensitive FID.

Extraction of gas from the oil is one of the critical stages of the process. When using the original ASTM D3612A method, it is required that extraction of most gas be made in high vacuum in a sealed glass vessel. Gas is accumulated and measured in a specially graduated tube. Then the gas is removed from the graduated tube through a membrane by a sealed syringe and is immediately injected into the GC. However, that method required the use of mercury. Since at present mercury is not used in most labs due to health hazard, two more mercury free gas extraction methods were developed.

One of these is the direct injection method, described in ASTM D3612B. Gas is extracted form the oil and analyzed within the GC. Initially developed in mid 1980s for this purpose, this method involves injecting oil samples into the chromatographer. When the chromatographer is started, the oil sample passes through a series of valves to the metal sphere of the evaporator. The carrier gas passes through the evaporator and extracts dissolved gas from the oil, which is then carried to the chromatographic column, were it is separated and passed through the sensor. The oil is washed from the surface of the sphere and is purged from the system before the next sample is tested.

Another new method, approved about a year ago, is called the vapor phase method, ASTM D3612C. This method has been used for dissolved gas analysis for almost a decade. However, the technology has become a standard only several years ago, when Jocelyn Jalbert of Hydro-Quebec improved the vapor phase method using Hewlett Packard instruments (now Agilent Technologies). The second method involves injection of a certain volume of gas into a clean sealed vacuum vessel. The sample is then sealed and agitated until equilibrium between vapor and gas is reached. After a certain period of time, an automatic sampler removes a part of the gas from the test vessel and injects it into the GC.

Although the ASTM D3612A has been known for a while, it is still widely used today. The advantage of the method is that it can be automated, reducing the risk of operator error while handling the sample in the process of preparation and injection.

Obviously, each method has its advantages and disadvantages. None of the methods ensures extraction of all gases from the oil. This is related to each gas individual solubility factor, which should be taken into consideration when determining concentration.

The advantage is that oil samples can be taken from most of the equipment without stopping the equipment for maintenance, which helps to reveal potential failures. Nevertheless, the alternative methods, which are more easily automated, are also coming into more use, as they prove their reliability.

To develop standards of gas analysis, laboratories must cooperate with commercial suppliers or prepare standards on their own, since at this time these standards have not been cleared though national standard authorities, such as the NIST.

Repeatability and accuracy of the tests is also very important, as small changes of several ppm may mean the difference between a developing problem which requires immediate attention and a stable parameter which requires no action at all. Efficient sampling process is extremely important to obtaining accurate data from DGA, since such gases as hydrogen or carbon monoxide can easily evaporate form the sample due to their low solubility in oil. To minimize gas losses, ASTM D3613 requires that samples be stored in gas-proof glass or metal vessels.

The typical gases generated by mineral oil and cellulose (paper and cardboard) in transformers are:

  • hydrogen H2;
  • methane CH4;
  • ethane C2H6;
  • ethylene C2H4;
  • acetylene C2H2;
  • carbon monoxide CO;
  • carbon dioxide CO2.

There are always some oxygen and nitrogen present in the oil, and their concentration depends on integrity of transformer sealing. Besides, there are other gases, such as propane, butane, buten, etc, but their content is not usually measured. Gas concentrations are indicative of various types of impending malfunctions and their severity.

For example, four categories of general failures have been described and characterized in table 1

Key gases Indicate these problems
Methane, ethane, ethylene and some acetylene Heat influencing the oil
Hydrogen, methane and some acetylene and methane Partial discharge
Hydrogen, acetylene and ethylene Arc drawing
Carbon monoxide and dioxide Heat influencing paper insulation

Electric discharges and inefficient cooling of paper insulation lead to the overheating and generation of carbon oxides.

As a rule, transformers retain most of the formed gases, making it possible to make general conclusions regarding insulation wear. Researching relative composition and ratios of the gases may provide more clues. The Rogers or Dornenburg methods are usually used for that purpose.

Severity of the impending failure may be assessed from the total volume of combustible gases (CO, H2, C2H2, C2H4, C2H6, CH4) and the rate of their generation.

Some gases are generated by natural aging of transformer insulation, making it important to discern between normal and excessive quantities of gas. Normal aging or generation of gas depends on transformer design, load and insulation type.

Normally, general indications of gas presence for all transformers are used to detect abnormalities. However, when scheduling new analyses, it is important to consider transformer age and the fact that transformers operated for several years may retain some residual gas.

Actual conclusions on condition of the transformer may be made based on extended gas analysis data. E.g. acetylene requires a lot of energy to form; this gas forms when oil is heated to over 700oC. Excessive oil heating leads to formation of some gas in low concentrations, however, higher concentrations indicate stable arcing, which is a serious operational problem, which will cause transformer failure unless the process is stopped.

The DGA method is an important instrument for detection and analysis of trends and it can be used both as a diagnostic tool, and as a tool to avoid transformer failure. When a large transformer fails, direct losses may be quite high (a transformer may cost over a million US dollars), and the collateral damage may also be significant; profit loss due to blackouts can be the least of the consequences. Transformer replacement, which can take up to one year if the damage is not significant, may cause immense profit loss and fines. However, if the failure is catastrophic, collateral damage is inevitable: it may include damage to nearby transformers, environmental problems due to spilling up to 20000 gallons of oil, or fire.

To avoid this unpleasant scenario, diagnostic of large power transformers should be annual, or at the very least once in three years. As problems are detected, frequency of tests should also be increased.

Insurance companies may also require a certain test schedule. They sometimes require annual oil test to facilitate continuous control.

The following examples illustrate how DGA may be used for detection of existing problems.

Example 1

Transformer information Transformer oil analysis* Results
McGrow Edison400 MVA330 kVGas coverMade in 1969 Hydrogen: 7 040 Ethylene was the key gas in this study, which indicated exposure of oil to very high temperature.
Methane: 17 700
Ethane: 4 200
Ethylene: 21 700
Acetylene: 165
Carbon monoxide: 67
Carbon dioxide: 1 040

• 25°C and 760 mm. Hg.

Example 2

Transformer information Transformer oil analysis* Results
Delta Star2.5 MVA44 kVRectangular core753 gallons of oilMade in 1991Failed after 4 years of operation Hydrogen: 10900 Ethylene and methane were the key gases. This indicated exposure of transformer oil to high temperatures. Acetylene content was high enough to suggest arcing in the oil. Large amounts of carbon dioxides indicated that paper was also involved in overheating.
Methane: 18400
Ethane: 4440
Ethylene: 24500
Acetylene: 3820
Carbon monoxide: 23800
Carbon dioxide: 36900

• 25°C and 760 mm. Hg.

Example 3

Transformer information Transformer oil analysis* Results
Power Hydrogen: 1980 Hydrogen levels were high, indicating a possibility of partial load; high levels of CO and CO2 indicate serious overheating of paper insulation.
11,46 MVA30 kVGas covered500 gallons of oilMade in 1940s Methane: 166
Ethane: 87
Ethylene: 205
Acetylene: 0
Carbon monoxide: 2990
Carbon dioxide: 58300

• 25°C and 760 mm. hg

Example 1

Core fixture was probably lose, and the core was either touching the winding or was very close to it. Undesired main and vortex currents cause local oil overheating.

Example 2.

Probable cause of transformer failure was one phase short circuiting to the ground. This resulted in damage to one of the coils. The analysis showed large acetylene quantity, which indicated possible arcing. The ratio of acetylene to ethylene pointed at oil overheating and/or arcing as possible cause of failure. It is probable that the failure was caused by damage to winding insulation, since relatively high concentrations of carbon monoxide and dioxide indicated insulation material degradation.

Example 3.

A technician notice that the transformer was covered in a cloud of steam in the rain. The test showed that thermal sensor was stuck, and the temperature in the tanks was over 200°C. It was also determined that the transformer was highly overloaded due to disproportion between two phases. The overload was estimated to have lasted for the last two years or so. Inspection of the internal transformer structure showed extensive crumbling and destruction of cellulose insulation. Again, the DGA indicated presence of mostly carbon monoxide and dioxide.

Gas analysis is apparently a very important part of efficiently running electrical equipment. As illustrated by the above examples, the DGA is the most important and efficient diagnostic tool for detection of a wide range of problems.

Characteristic of Wastewater and its analysis

Wastewater containing chromium and other heavy metals, is highly toxic effluents which require high-quality and efficient purification. Such effluents formed during electroplating, other types of chemical, electrochemical surface treatment of metal products such as chromium-plating, nickel-plating, copper-plating, zinc-plating, cadmium-plating and also during some technological processes. These effluents compose 40-60% of the total wastewater generated in the enterprises.

Intensifier of technological processes

The required degree of wastewater treatment shall be based on the effluent requirements and water quality standards established by the responsible province, state agency and/or appropriate federal regulations including discharge permit requirements.

According to State Standard for the wastewater when it arrive at the city sewage treatment plant should not have: pH value less than 6.5 and high than 8.5, the content of hexavalent chromium (Cr6+) in excess of 0,1 mg/dm3; trivalent chromium (Cr3+) – 2,5 mg/dm3, cooper – 0,5 mg/dm3, nickel – 0,5 mg/dm3, zinc – 1 mg/dm3, iron – 0,5 mg/dm3, cadmium – 0,1 mg/dm3, and other impurities up to maximum permissible concentration (MPC).

There are a lot of different installations for sewage treatment. One of them is AVS-100 – Intensifier of Technological processes by PC GlobeCore.

For concentrations of contaminants these wastewaters can be divided into two main groups:

  • low-concentration wastewater;
  • spent and concentrated solutions of electrolytes.

By the nature of the major impurities of wastewater, their volumes and revenues  when they arrive at the sewage treatment plant divided into two types:

  • chromium-containing waste water (containing acids, alkalis, and principally a chromium compound);
  • acid-alkaline wastewater (containing acids, alkalis, and salts of heavy metals).

The main quantity of these types of wastewater comprise scouring water, which composition is formed by diluting in water processing solutions, as well as coating and further washing products.

These waste water arrives at purification plants during the all working day continuously, and spent process solutions and electrolytes with a high concentration of salts of heavy metals arrives at purification plants periodically.

In this case chromium-containing waste water comprise 15-20% from total amount of sewage, acid-alkaline wastewater – 50-70%.

The main components which contain the wastewater on different enterprises are chromium, copper, zinc, iron, nickel, cadmium.

Their content and the amount determined by the concentration of electrolytes in processing tank for products covering, also by the mode of product flushing, its amount and configuration.

The concentration of Cr6+ in the chromium-containing wastewater is changed over a wide range from 10 to 800 mg/dm3, and can achieve 1000 mg/dm3 when entering to the scouring sewage of spent solutions and electrolytes; pH value is changed in the range from 2 to 7. In this case the chromium-containing wastewater may contain small number of other metals (10-20 mg/dm3). Contents of Cu, Ni, Zn, Fe, Cd in acid-alkaline wastewater also is changed over a wide range and can be achieved: 5-300; 10-250; 2-350; 10-600; 10-150 mg/dm3, рН 3-9 accordingly.

On basis of the fuller information about wastewater content authors obtained  from the enterprises which are produce equipments for the food industry and its inspection. That information was used for the development of effective methods of wastewater treatment by using AVS (intensifier of technological processes).

The analysis showed that the major changes in the concentrations of pH value of the effluents takes place by reason of the absence of intermediate containers (10-50 times), that would provide a reliable and efficient operation of treatment facilities with the required quality of cleaning.

In research and development of new and effective methods of treatment using Intensifier of Technological Processes AVS-100 all this information was taken into account.

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Regeneration of used oil

Used oil regeneration technologies

Over time, oil accumulates oxidation products, contaminants and impurities which drastically reduce its quality. Contaminated oil can no longer meet quality requirements and must be changed. Waste oil is collected and regenerated to retain valuable basic materials.

Oil cannot be recycled at petroleum processing plants with fossil oil, since additives contained in the oil disrupt oil processing machinery.

Depending on the actual regeneration process used, 2 or 3 basic oil fractions are produced; these can be mixed with additives to produce commercial oil (motor, transmission, hydraulic oils and plastic lubricants). Average yield of regenerated oil from waste oil containing 2 – 4% solids and water and up to 10% fuel, is 70 – 85% depending on the regeneration process used.

Regeneration of waste oil may involve various technologies, based on physical, chemical of combined physical and chemical processing. All of these processes are aimed to remove aging products and contaminants from the oil. The following sequence is normally used: mechanical removal of free water and solids from oil, evaporation or vacuum distillation and coagulation. If the above prove insufficient, chemical oil regeneration is used; those methods usually involve complex equipment and high costs.

Physical methods allow removal of solids particles, microscopic water droplets and some tar and coke material; evaporation removes some volatile impurities. Oil is processed by gravity, centrifugal force, and sometimes by electric or magnetic fields and vibration; other methods include filtration, water wash, and vacuum distillation. Physical methods also include various mass and heat exchange processes used to remove hydrocarbon oxidation products, water and volatile fractions.

Regenerated transformer oil by GlobeCore`s plants

Regenerated transformer oil by GlobeCore`s plants

Settling is the simplest method, based on natural gravity settling of particles and water. Depending on the degree of contamination and time allotted for purification, settling can either be used as a standalone method, or as preparation for filtration and centrifuge. The drawback of this method is the long time it takes and the large size of particles that can be removed (50 – 100 micron).

Filtration is a process to remove solid contaminants and tars by making the oil pass through mesh or porous filters. Common filtering media are metal and plastic meshes, felt, fabric, composite material and ceramics. Most facilities combine an increased number of strainers for basic filtration with the second stage of fine filtration.

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