2016 International Conference on Computation of Power, Energy Information and Communication (ICCPEIC) Study of Dissolved Gas Analysis for Pre­ Determination of Faults in Transformers Nikhileshwar P. Adhikari Amit Gupta Triparna Nandy PG Scholar Assistant Professor GGCT, Jabalpur Assistant Professor LNCT Group Of College GGCT,Jabalpur India India nandytriparnal90lgmail.com Bhopal, India nikhil adhikari0lrediffmail.com amit.hvps0lgmail.com One of the best methods of detecting certain This de-gradation can lead to pre-mature failure of problems which can lead to failure of the transformer is the transformer. The two important functions of the Abstract - Dissolved Gas Analysis (DGA). For diagnosing fault oil are to provide cooling and electrical insulation. condition on oil filled insulation, one of the most recent techniques developed is Dissolved Gas Analysis. The chemical analysis of the generated gases is known as Dissolved Gas Analysis or DGA. For DGA, oil sample from the transformer has to be removed which can be Oil used in transformer is a mixture of Hydro-carbons. Lower order of Hydro-carbons like Methane, Acetylene, Ethane, Ethylene etc. are produced with some permanent gases like Carbon done without de-energization of the transformer easily. Di-oxide, Carbon Mon-oxide and hydrogen during Then oil the process of degradation. Failures are inevitable in paper oil filled equipment such as power transformer if presents complete DGA study of 12.5 MVA 132/33KV, proper care is not taken. The mixture of hydrocarbons by sample using is gas analyzed chromatography in the technique, laboratory. This EMCO makes Transformer: at 132 KV SIS Srinagar (M.P.). The data are analyzed over a period of 2006 to 2012. The DGA results by different standard methods are compared. and permanent gases is sealed environment can cause an explosion. In the running condition, proper monitoring is needed on the concentration of these explosive gases [7] . Initially the generated gases will Keywords - Dissolved Gas Analysis (DGA), Parts per dissolve in the oil. When the generated gases million (PPM), Gas Chromatography (GC), Rogers Ratio increases in its volume, more of it will dissolve into Method. the oil. Eventually a stage will come when the oil will be completely saturated with the dissolved gases and I. Oil is used gas in the oil so it will come out as free gas. By insulation purpose. Mineral oil de-gradation in oil evaluating the amount of generated gas present and filled transformers is a major concern. Analysis of oil the rate of gas generation, abnormal condition can be sample detected. maintenance transformers transformer tool for is for any further increase cannot be contained as dissolve and of in INTRODUCTION useful, cooling predictive determining health and of transformer. Ageing of the oil, overheat, overvoltage, II. METHEDOLOGY environmental conditions and numerous unknown DGA: It is an effective as well as practical method factors are responsible for the oil degradation [2] . which helps in the detection of incipient faults along [Type text] 978-1-5090-0901-5/16/$31.00 ©2016 IEEE 634 Tripama Nandy et af: Study of Dissolved Gas Analysis for Pre-Determination of Faults in Transformers with its order of severity. After commissioning of the transformer oil using vacuum extraction method transformer, DGA shall be repeated once in a month For extraction of gases whereas in case of transformer which has been extraction, repaired, DGA should be carried out in a week soon extraction can be used. Disadvantages of this method after decommissioning and then after about 3 months. are it is very expensive and also time taking. Due to DGA is very helpful as faults are identified and limitations necessary actions are taken before any catastrophic hydrogen failure occurs. [6] spectroscopy have been developed. Both headspace of GC, on-line two from the sampling new monitoring oil, and techniques and stripper vacuum namely photo acoustic For the improvement in reliability and power of these methods requires less time as compared to availability, DGA plays an important role. On the Gc. For analyzing dissolved gases in insulating oil, basis of results obtained, investigation has become GC has been used for the last 60 years. After IEC, easier and problems thus are resolved in less time [5] . IEEE and ASTM published relevant guidelines, this Many industries are now aware of this tool and using method became more popular. it for reduced maintenance and reduced cost of methods, GC is accepted as the best method for repairs of power transformers. measuring the concentration of gases dissolved in Gas chromatography: One of the most widely used transformer oil. In the laboratory environment, GC methods analysis is successfully conducted [7] . is Gas Chromatography (GC) . Gas Among the three Chromatography apparatus of Chernito Company is used in MPPTCL. For the separation of different complex mixtures, GC is used. From the operating transformers, oil samples are collected and taken to the laboratory for the gas extraction and analysis. Oil sample is taken from the transformers and transported to the laboratory using syringes, flexible metal cans, and special glass bottles or in the calibrated stainless III. ANALYSIS METHODS steel cylinders. From the bottom of the tank, oil Rogers Ratio Method: In this method, A 4 digit ratio samples are usually taken. code is generated from the five fault gases namely This method for DGA is used once in a year only as hydrogen, methane, ethane, ethylene and acetylene it is a costly process. for determining 15 diagnosis rules for transformer conditions. Table 1 Roger's ratio gas Fig.1 Extraction of dissolved gases from RATIO CODE CH4/H2 1 C2HJCH4 2 C2HJC2H6 3 C2H2/C2H4 4 978-1-5090-0901-5/16/$31.00 ©2016 IEEE 635 2016 International Conference on Computation of Power, Energy Information and Communication (ICCPEIC) 1. If all the four ratios are equal to zero then it remaining ratios equal to zero, indicates no fault. energy discharge (arc with power flow through). 2. If code 2=5, in other words when the ratio of 9. If code 3 is equal to zero, in other words when the ethane to methane is equal to 5 and remaining three ratio of ethylene to ethane is equal to 1 with codes are zero then it indicates partial discharge of remaining ratios equal to zero, it indicates insulated low energy density or hydrolysis. conductor overheating. 3. If code 1=1 and code 2=5, in other words when the lO.lf code 3 is equal to one and code 4 also equal to ratio of methane to hydrogen is equal to one and that 1, in other words when the ratio of ethylene to ethane of ethane to methane is equal to 5 respectively with is 1 and ratio of acetylene to ethylene is also equal to remaining two ratios equal to zero, it indicates partial 1 with remaining two ratios equal to zero, it indicates discharge of high density which is possible with complex thermal hotspot and conductor overheating. tracking. 11.1f code 1 is equal to one and code 4 is equal to 4. If code 2=5 and code 3=1, in other words when the one, in other words when the ratio of methane to ratio of ethane to methane is equal to 5 and ratio of hydrogen is 1 and ratio of acetylene to ethylene is ethylene to ethane is equal to 1 with remaining two also 1 with remaining two ratios equal to zero, it ratios zero, indicates then it indicates coincidental partial coincidental thermal it indicates high hotspot and low discharges and conductor overheating. energy discharge. 5. If code 2=5 and code 4=1, in other words when the 12.1f code 2 is equal to one, in other words when the ratio of ethane to methane is equal to 5 and that of ratio of ethane to methane is equal to 1 with the acetylene to ethylene is equal to 1 with remaining remaining three ratios equal to zero, it indicates two ratios equal to zero, it then indicates partial thermal fault of low temperature range less than 150 discharges of increasing energy density. degree Celsius. 6. If code 1 is greater than 1 but less than 2, in other 13. If code 2 is greater than zero but less than 2 and words when the ratio of methane to hydrogen is code 4 is equal to l,in other words when the ratio of greater than 1 but less than 2 and remaining ratios are ethane to methane is greater than zero but less than 2 zero, and ratio of acetylene to ethylene is 1 with remaining it then indicates low energy discharge (flashover without power flow through). two ratios equal to zero, it indicates thermal fault of 7. If code 1 is greater than 1 but less than 2 and code temperature range from 100 degree Celsius to 200 3 is equal to 1, in other words when the ratio of degree Celsius. methane to hydrogen is greater than 1 but less than 2 14. If code 2 is equal to one and code 3 is also equal and ratio of ethylene to ethane is equal to 1 with to one, in other words when the ratio of ethane to remaining ratios equal to zero, it indicates low energy methane is equal to 1 and ratio of ethylene to ethane discharge (continuous sparking to floating potential). is 1 with remaining two ratios equal to zero, it 8. If code 1 is greater than 1 but less than 2 and code indicates thermal fault of temperature range from 150 3 is equal to 2, in other words when the ratio of degree Celsius to 300 degree Celsius. It occurs due to methane to hydrogen is greater than 1 but less than 2 overheating of copper due to eddy currents. and ratio of ethylene to ethane is equal to 2 with [Type text] 978-1-5090-0901-5/16/$31.00 ©2016 IEEE 636 Tripama Nandy et af: Study of Dissolved Gas Analysis for Pre-Determination of Faults in Transformers 15. If code 2 is greater than 1 but less than 2 and code When the ratio of acetylene to ethylene is not 3 is equal to 2, in other words when the ratio of significant (code 1=not significant), ratio of methane ethane to methane is greater than 1 but less than 2 to hydrogen is greater than 1 (code 2 >1) and ratio of and ratio of with ethylene to ethane is less than 1 (code 3 <1) it it indicates indicates thermal fault of temperature less than 300 ethylene to ethane is equal to 2 remaining two ratios equal to zero, thermal fault of temperature range from 300 degree degree Celsius. Celsius to 700 degree Celsius. It occurs due to bad When the ratio of acetylene to ethylene is less than contacts/joints. [3] 0.1 (code 1<0.1), ratio of methane to hydrogen is IEC Basic Ratio Method: This method has originated greater than 1 (code 2>1) and ratio of ethylene to from the Rogers Ratio Method, except that the ratio ethane is in the range of 1 to 4 (1<code 3 <4) it of ethane to methane is not included in this method as indicates thermal fault of temperature between 300 it only indicated a limited temperature range of degree Celsius to 700 degree Celsius. decomposition. When the ratio of acetylene to ethylene is less than 0.22 (code 1 <0.22), ratio of methane to hydrogen is greater than 1 (code 2>1) and ratio of ethylene to Table 2 IEC basic ratio gas Ratio Code ethane is greater than 4 (code 3>4) it indicates C2H2/C2H. 1 thermal fault for temperature greater than 700 degree CH./H2 2 C2HJC2H. 3 When the ratio of acetylene to ethylene is not significant (code 1=not significant), ratio of methane to hydrogen is less than 0.1 (code 2<0.1) and ratio of ethylene to ethane is less than 0. 2 (code 3 <0.3) it Celsius. Increasing value of acetylene may indicate that the hot spot temperature is higher than 1000 degree Celsius. [4] Key Gas Method: Table 3 key gas parameter Gas Normal Abnormal Tnterpretation H2 <150 ppm >1000 ppm Arcing, Corona CH. <25 ppm >80 ppm Sparking C2H. <10 ppm >35 ppm Local Overheating C2H. <20 ppm >100 ppm Severe Overheating CO <500 ppm >1000 ppm Severe Overheating When the ratio of acetylene to ethylene is in the CO2 <1000 ppm >15000 ppm Severe Overheating range of 0.6 to 2. 5 (0.6<code 1>2.5), ratio of methane N2 1-10% N.A to hydrogen is in the range of 0.1 to 1 (0.1 <code 2<1) O2 0.2-3.5% N.A>0.5% indicates partial discharges. When the ratio of acetylene to ethylene is greater than 1(code 1>1), ratio of methane to hydrogen is in the range of 0.1 to 0.5 (0.1 <code 2<0.5) and ratio of ethylene to ethane is greater than 1 (code 3 <1) it indicates discharges of low energy. and ratio of ethylene to ethane is greater than 2 (code Combustibles IV. DATA OBTAINED FROM MPPTCL 3 <2) it indicates discharges of high energy. 978-1-5090-0901-5/16/$31.00 ©2016 IEEE 637 2016 International Conference on Computation of Power, Energy Information and Communication (ICCPEIC) Table 4 data collected from MPPTCL Hz(in Date of Testing parts per million ppm) Oz(in parts per million ppm) COz(in parts per million ppm) CzH.(in parts per million ppm) CzH. (in parts per million ppm) CzHz(in parts per million ppm) CO(in CH.(in parts per million parts per million ppm) ppm) p+p (in parts per million ppm) TOTAL (in parts per million ppm) 02/01106 6 19559 1352 2 I NIL 17 NIL 2 20939 30111106 2.8625 0 795.3932 0.6463 0.2897 0.0022717 64.096 1.6356 0.3746 865.5007 14/02/07 2.6905 5305.125 1401.0163 0.6675 0.7763 0 29.1343 1.2301 1.126 674.7665 12/06/07 0.9062 11030.57 651.7298 0.6249 0.2312 0.020202 37.841 0.7889 0.2481 11722.955 05/03/08 1.4004 10354.9902 552.5699 0.00016324 0.075920 0.0043099 35.1829 0.6540 0.3462 10945.2239 01104/09 0.7966 8760.1555 261.1016 0.000024859 0.0005662 0.076823 9.4063 0.3298 0.1128 9031.9740 30/07/10 2.9941 2676.6658 560.195 0.6411 0.1154 0.00092215 8.6342 0.4447 0.2975 3249.9895 17/02/11 0.5005 3776.0119 490.1201 0.9172 0.093243 0.0062040 0.7331 0.2446 0.5729 4269.1997 19112/11 87.9727 -- 0.0 1978.380 0.9659 0.00 168.0650 9.1488 0.00 2244.5324 05110/12 0.8443 -- 1169.000 0.8917 0.4800 0.0797 135.1660 1.3775 0.2769 1308.1169 Table 5 the Result Obtained according To ROGER'S RA no METHOD Dates Code 1 Code 2 Code 3 Code 4 02.01.06 NiIl6 IINil 211=2 NiIl2 30.11.06 1.6356/2.8625=0.57 0.2897/1.6356=0.177 0.6463/0.2897=2.2309 0.00227717/0.6463=0.035 14.02.07 1.2301/2.6905=0.457 0.7763/1.2301=0.631 0.6675/0.7763=0.8598 0/0.6675=0 12.06.07 0.7889/0.9062=0.87 0.2312/0.7889=0.293 0.6249/0.2312=2.702 0.020202/0.6249=0.03 05.03.08 0.6540/1.4004=0.467 0.075920/0.6540=0.116 0.00016324/0.075920=0.02 0.0043099/0.00016324=26.40 01.04.09 0.3298/0.7966=0.414 0.0005662/0.3298=0.017 0.000024859/0.0005662=0.043 0.076823/0.000024859=3090.349 30.07.10 0.4447/2.9941=0.148 0.1154/0.4447=0.259 0.641110.1154=5.555 0.00092215/0.6411=0.00143 17.02.11 0.2446/0.5005=0.4887 0.093243/0.2446=0.38 0.9172/0.093243=0.98366 0.0062040/0.9172=0.0067 19.12.11 9.1488/87.9727=0.1039 0.9659/9.1488=0.1055 1978.380/0.9659=2048.22 0.00/1978.380=0 05.10.12 1.3775/0.8443=1.63 0.4800/1.3775=0.348 0.8917/0.4800=1.8577 0.0797/0.8917=0.8937 [Type text] 978-1-5090-0901-5/16/$31.00 ©2016 IEEE 638 Triparna Nandy et af: Study of Dissolved Gas Analysis for Pre-Determination of Faults in Transformers V. TEST RESULTS AND ANALYSIS H2 Result Obtained according To Roger's Ratio Method: collected data of failed transformer is checked according to roger's ratio method. It is found that on 100 I 5� 1\, '" .. .. .. .. .. i o..-ioooooo..-i..-i NO.,tNu-i..-iO"aiu-i date 05.10.12, it indicates high energy discharge - H2 0('1) ........00('1) .. ...... .. 0 .. which was the cause of failure of the transformer. Fig 3. Graph for H2 from 2006 to 2012. The results are presented in table 5. Result Obtained According To IEC Basic Ratio Method: Collected data of failed transformer is checked according to IEC basic ratio method: It is found that on date 19.12.11, it indicates high energy discharge which was the cause of abnormality in the transformer. The results are presented in table 6 The above graph indicates that H2 is almost constant over a period of 4 years , it increases in 2011 due to internal arcing and corona discharge. During overhauling of transformer some loose connection were found and the same were rectified by soldering and tightning of bushing to internal winding connection. hereunder Table 6 Collected data of failed transformer is checked Dates Code 1 Code 2 Code 3 02.01.06 0 0 2 30.1l.06 0.035 0. 57 2.2309 14.02.07 0 0.457 0. 8598 12.06.07 0.03 0. 87 2.702 05.03. 08 26.40 0.467 0.02 01.04.09 3090.349 0.414 0.043 30.07.10 0.00143 0.148 5.55 17.02.11 0.0067 0.4887 0.98366 19.12.11 0 0.1039 2048.22 05.10.12 0. 8937 l.63 l. 8577 02 40000 �------ 20000 +t-----­ o +-��r_���� - 02 Fig 4. Graph for O2 from 2006 to 2012. The graph shows the content of oxygen decreases due to combustion and ingress of particle impurity. The oil flirtation was done in November 2006 and the oxygen increase, it further continuously decreases over a period from 2007 to 2012 . The oil filtration is recommended at present. C02 Result Obtained According To Key Gas Method: 2000 According to key gas method , The cause of failure of 1000 this transformer was severe overheating as C2H4 gas o - CO2 is much more than normal value which is 100 parts per million(ppm). Fig 5. Graph for CO2 from 2006 to 2012. 978-1-5090-0901-5/16/$31.00 ©2016 IEEE 639 2016 International Conference on Computation of Power, Energy Information and Communication (ICCPEIC) The above graph indicates that COz has decreased in November 2006 due to oil filtration.But due to overloading in February 2007, it has again increased 0. 1 causing severe overheating. In June 2007, the problem 0.05 of overloading was solved and COz decreased.But o again load increased in October 2012 I A causing overheating as well increase in concentation of COz. Fig 8. Graph for CzHz from 2006 to 2012. due to overloading its concentation increased causing 4000 severe overheating. Oil filtration is recommended at 2000 o i i i i i i i ZS i - CzH4 co Fig 6. Graph for CZH4 from 2006 to 2012. This graph shows that CZH4 was almost constant from January 2006 to February 2011.Suddenly in December 2011 concentration present. increased 200 ,----------------10 � I¢; "7 • • t, - co causing severe overheating. Remedial actions were then taken Figure 9. Graph for CO from 2006 to 2012. to decrease its concentration. This graph indicates that concentration of CO has increased from January 2006 to November 2006 as a result of overloading.Due to some remedial actions it 2 decreased to some extent. But again load increased in I � S?S; .. December 2011 as a result its concentarion also C, increased causing severe overheating. .. , 0 ""';000000 ""'; ""'; NO.,tNu-i ""';o,,_: criu-i om ...... ...... 0 om ...... ...... o Fig 7. Graph for CZH6 from 2006 to 2012. This graph indicates that CZH6 decreased initially from January 2006 to November 2006 due to oil 10 : 1�""",i,i6" T--------------��- ,....; ,....;N�rti.,t.._: NNO 0 ...... 000000 ...... ...... NO.,tNu-i ""';o,,_: criu-i filtration and then slightly increased in February 2007 causing local overheating. Due to remedial actions taken in time its concentration decreased. This graph shows that initially concentation of CzHz was under normal operating limits but om ...... ...... oom ...... ...... 0 Fig 10. Graph for CH4 from 2006 to 2012. This graph indicates that CH4 increased in December 2011. [Type text] 978-1-5090-0901-5/16/$31.00 ©2016 IEEE 640 Triparna Nandy et af: Study of Dissolved Gas Analysis for Pre-Determination of Faults in Transformers The cause behind this was sparking. Prior to 2011 it severe overheating etc are predicted by DGA. During was under normal operating limits. ovehauling of transformer, loose connections should be p+p 3 2 1 0 rectified by soldering and tightning of bushing to internal .-I .-I connection, addition of DBPC Powder, oil reclaimation and other remedial actions I�,�, � � r-- r-- 00 (j) 0 .-I 0 0 0 0 C! 0 .-I .-I winding should be taken to decrease the concentration of gases in oil. It will increase the active life span of the -p+p transformer. N .-I .-i .-i N <.0 M � r' N N ci C! .-I 0 0 C! C! 0 C! .-I .-I N 0 � N LJ") .-I 0 r-- (j) LJ") 0 M .-I .-I 0 0 M .-I .-I 0 VII. REFERENCES Figure 11. Graph for P+P from 2006 to 2012. This graph shows that concentration of P+P i. e [1] Rahul Pandey and M. T. Deshpande, "Dissolved propylene and propane has decreased over the years. Gas Analysis (DGA) of Mineral Oil Used in Transformer." International Journal of Application or Innovation in Engineering & Management (IJAIEM) VI. CONCLUSION Volume 1, Issue 2, October 2012. 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