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Bulletin of Electrical Engineering and Informatics
Vol. 10, No. 5, October 2021, pp. 2327~2336
ISSN: 2302-9285, DOI: 10.11591/eei.v10i5.3131 ๏ฒ2327
Journal homepage: http://beei.org
Analysis of thermal models to determine the loss of life of
mineral oil immersed transformers
Mohammad Tolou Askari1
, Mohammad Javad Mohammadi2
, Jagadeesh Pasupuleti3
, Mehrdad
Tahmasebi4
, Shangari K Raveendran5
, Mohd Zainal Abdin Ab Kadir6
1,2
Department of Electrical Engineering, Semnan Branch, Islamic Azad University, Semnan, Iran
3,5
Institute of Sustainable Energy, Universiti Tenaga Nasional (UNITEN), Kajang, Malaysia
4
Department of Electrical Engineering, Ilam Branch, Islamic Azad University, Ilam, Iran
6
Institute of Power Engineering (IPE), Universiti Tenaga Nasional (UNITEN), Kajang, Malaysia
6
Centre for Electromagnetic and Lightning Protection Research (CELP), Faculty of Engineering, Universiti Putra
Malaysia, Serdang, Malaysia
Article Info ABSTRACT
Article history:
Received Dec 2, 2019
Revised May 2, 2021
Accepted Jul 14, 2021
Hot spot as well as top oil temperatures have played the most effective
parameters on the life of the electrical transformers. The prognostication of
these factors is very vital for determining the residual life of the electrical
transformers in the transmission and distribution systems. Thus, an accurate
mathematical method is required to calculate the critical temperature such as
hot spot and top oil temperature based on the different types of thermal
models. In this study calculates the service life of the transformers based on
an accurate top oil temperature. Accordingly, An approach solution is given
for calculating the thermal model. Also, findings are validated with true
temperatures. Finally, this method is implemented on 2500 KVA electrical
transformer.
Keywords:
Electrical transformer
Hot spot temprature
Numerical analysis
Thermal model
This is an open access article under the CC BY-SA license.
Corresponding Author:
Mohammad Tolou Askari
Department of Electrical Engineering, Semnan Branch
Islamic Azad University, Semnan, Iran
Email: m.askari@semnaniau.ac.ir
1. INTRODUCTION
Electrical transformers the facilities in electrical power networks that the correct operation of it has
played main role in providing reliability of these systems. By noticing the costs of transformers and
permanent connection of transformers to transmission and distribution systems, any action to increase the life
cause improvement in the operation of power systems. Life of the electrical transformer and loading
capabilities of this facilities depend on several parameters. Oil and paper in transformers are two insulation
materials, that the integrity of them warranties the life of transformers. Hot spot temperature (HST) and top
oil temperature (TOT) are two criteria to evaluate the integrity of these two insulation materials and
transformers as important facility in power network [1]-[3]. These criteria determine the temperature
limitation of transformer for loading capability, for example the IEEE standard suggests that the TOT rise
over ambient temperature 65ยฐC and depending on it has considered 110ยฐC for HST [4]-[6]. It means that
increasing the temperature of transformer over this standard value causes the degradation of insulation life of
transformer. According to research, from 90ยฐC to 110ยฐC, the aging rate of tensile strength approximately
doubles every 5ยฐC to 10ยฐC temperature rise [2], [3], [7]-[9]. A. A. Taheri, A. Abdali and A. Rabiee [10] a
thermal resistance with solar radiation is used to explain the heat transfer theory in transformer. The effect of
๏ฒ ISSN: 2302-9285
Bulletin of Electr Eng & Inf, Vol. 10, No. 5, October 2021 : 2327 โ€“ 2336
2328
long term ambient temperature was investigated in [11], [12]. There are some dynamic factors in oil
immersed transformer such as ambient temperatures, winding losses and oil viscosity of transformer [3],
[13]. In this article, two thermal models, classic thermal model as famous and reliable thermal model and
dynamic thermal model as improved thermal model, has been used. Moreover, TOT and HST is calculated
for both thermal model by IEEE standard method that has been available in [3] and also these temperatures
are calculated by proposed method. To validate and show the tolerance of numerical technique, the results of
models compared with measured value.
2. LITERATURE REVIEW
2.1. Thermal model
2.1.1. Classic thermal model
Thermal model is used to estimate the critical temperature of the transformer. The classic one was
given base on the heat generated and distributed in the windings and oil of transformer [3], [9]. Figure 1
shows temperature distribution in the transformer.
Figure 1. The temperature distribution in the transformer
The classic thermal model is used by a differential equation as [3]:
๐‘‡0
๐‘‘๐œƒ๐‘ก๐‘œ๐‘
๐‘‘๐‘ก
= โˆ’๐œƒ๐‘ก๐‘œ๐‘ + ๐œƒ๐‘ข + ๐œƒ๐‘Ž๐‘š๐‘ (1)
The solution as:
๐œƒ๐‘ก๐‘œ๐‘ = (๐œƒ๐‘ข + ๐œƒ๐‘Ž๐‘š๐‘ โˆ’ ๐œƒ๐‘ก๐‘œ๐‘๐‘–)(1 โˆ’ ๐‘’
โˆ’(
๐‘ก
๐‘‡0
)
) + ๐œƒ๐‘ก๐‘œ๐‘๐‘–โ€ (2)
and
๐œƒ๐‘ข = ๐œƒ๐‘“๐‘™ [
๐ผ๐‘๐‘ข
2 ๐‘…+1
๐‘…+1
]
๐‘›
(3)
๐‘‡0 =
๐ถ๐œƒ๐‘“๐‘™
๐‘ƒ๐‘“๐‘™
(4)
where: ๐œƒ๐‘‡๐‘‚๐‘ƒ=Top-oil rise over ambient temperature (C)
๐œƒ๐‘ข=Ultimate top-oil rise for load L (C)
๐œƒ๐‘–=Initial top-oil rise for t=0 (C)
๐œƒ๐‘“๐‘™=Top-oil rise over ambient temperature at rated load
๐‘‡0=Time constant
๐‘›=Oil exponent
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Analysis of thermal models to determine the loss of life of mineral oil โ€ฆ (Mohammad Tolou Askari)
2329
๐ผ=Specified load
๐ผ๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘=Rated load
๐ผ๐‘๐‘ข=Ratio of specified load to rated load
The transient rise of the hottest spot of the winding higher than the upper limit of the oil temperature is
determined by the following formula [3]:
๐›ฅ๐œƒ๐ป = (๐›ฅ๐œƒ๐ป,๐‘ˆ โˆ’ ๐›ฅ๐œƒ๐ป,๐‘–) [1 โˆ’ ๐‘’๐‘ฅ๐‘
โˆ’๐‘ก
๐‘‡0 ] + ๐›ฅ๐œƒ๐ป,๐‘– (5)
That the initial value for hot-spot temperature rise over top-oil temperature is given by:
๐›ฅ๐œƒ๐ป,๐‘– = ๐›ฅ๐œƒ๐ป,๐‘…๐ผ๐‘–,๐‘๐‘ข
2๐‘š
(6)
The maximum hot spots are as follows:
๐›ฅ๐œƒ๐ป,๐‘ˆ = ๐›ฅ๐œƒ๐ป,๐‘…๐ผ๐‘ˆ,๐‘๐‘ข
2๐‘š
(7)
The nominal hottest temperature spot value is given by:
๐›ฅ๐œƒ๐ป,๐‘… = ๐›ฅ๐œƒ๐ป/๐ด,๐‘… โˆ’ ๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘… (8)
where: ๐›ฅ๐œƒ๐ป=Hottest temperature spot rise over top oil temperature (C)
๐›ฅ๐œƒ๐ป,๐‘ˆ=Maximum hottest temperature spot rise over maximum oil temperature for load(C)
๐›ฅ๐œƒ๐ป,๐‘–=Initial hottest temperature spot rise over top oil temperature for t = 0 (C)
๐‘‡0=time constant of the transformer winding (h)
๐‘ก=Loading time (h)
๐›ฅ๐œƒ๐ป,๐‘…=Nominal hot spot rising above maximum oil temperature (C)
๐ผ=Current of load per unit
M=The exponent determines the non-linearity as shown in Table 1
The manufacturer has specified the amount of n for each mode of cooling. The amounts of n and m
for each cooling method are shown in Table 1 [3].
Table 1. Exponents for temperature determination formulas
cooling M N
OA 0.8 0.8
FA 0.8 0.9
Non-directed FOA or FOW 0.8 0.9
Directed FOA or FOW 1 1
HST will be calculated by (9).
๐œƒ๐ป๐‘†๐‘‡ = ๐›ฅ๐œƒ๐‘‡๐‘‚๐‘‡ + ๐›ฅ๐œƒ๐ป๐‘†๐‘‡ + ๐œƒ๐‘Ž๐‘š๐‘ (9)
2.2.2. Dynamic thermal model
Firstly, A dynamic thermal model of electrical transformer has been offered by Swift based on the
principals of heat transfer theory [14]-[17] after that an improved model has been introduced by Susa by
assuming the non-linear thermal oil resistance base on swiftโ€™s approach. In Susaโ€™s model the variations of
viscosity with temperature were considered [9]. TOT of dynamic thermal model is governed by (1).
1+๐‘…ร—๐พ2
1+๐‘…
ร— ๐œ‡๐‘๐‘ข
๐‘›
ร— ๐œƒ๐‘“๐‘™ = ๐œ‡๐‘๐‘ข
๐‘›
ร— ๐œ0 ร—
๐‘‘๐œƒ๐‘œ๐‘–๐‘™
๐‘‘๐‘ก
+
(๐œƒ๐‘œ๐‘–๐‘™โˆ’๐œƒ๐‘Ž๐‘š๐‘)1+๐‘›
๐œƒ๐‘“๐‘™
๐‘› (10)
Oil viscosity is added as a parameter. This can be determined by [18].
๐œ‡๐‘๐‘ข = ๐‘’
[(
2797.3
๐œƒ๐‘ก๐‘œ๐‘+273
)โˆ’(
2797.3
๐œƒ๐‘“๐‘™+273
)]
(11)
where: ๐พ=load current per unit
๐‘…=proportionality of load to no-load losses
๐œ0=top oil time constant, (min)
๐œƒ๐‘“๐‘™=rated top oil rise over ambient, (K)
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๐œƒ๐‘œ๐‘–๐‘™=top oil temperature gradient, (K)
๐œƒ๐‘Ž๐‘š๐‘=ambient temperature, (K)
๐œ‡๐‘๐‘ข=oil viscosity per unit
๐‘›=empirical constant, the amount of n has been specified for each cooling mode in Table 2 [2].
Tabel 2. Experimental value of n
Oil circulation n
With cooling without cooling
Initial oil circulation, Speed=0, (cold start) ONAF/OFAF ONAN ONAN
0.5 0 0.25
โ€œInitial oil circulation, Speed>0, (transformer on load)โ€ 0.2 0.25 0.25
HST of dynamic thermal model is given as [19]:
[๐พ2
ร— ๐‘ƒ๐‘ค๐‘‘,๐‘๐‘ข] ร— ๐œ‡๐‘๐‘ข
๐‘›
ร— ๐›ฅ๐œƒโ„Ž๐‘ ,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘ = ๐œ‡๐‘๐‘ข
๐‘›
ร— ๐œ๐‘ค๐‘‘,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘ ร—
๐‘‘๐œƒโ„Ž๐‘ 
๐‘‘๐‘ก
+ (
(๐œƒโ„Ž๐‘ โˆ’๐œƒ๐‘œ๐‘–๐‘™)๐‘›+1
๐›ฅ๐œƒโ„Ž๐‘ ,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘
๐‘› ) (12)
Pwd,pu, is the load lossโ€™s dependence on temperature that can be determined by (13)
๐‘ƒ๐‘ค๐‘‘,๐‘๐‘ข = ๐‘ƒ๐‘‘๐‘,๐‘๐‘ข ร— (
๐œƒโ„Ž๐‘ +๐œƒ๐‘˜
๐œƒโ„Ž๐‘ ,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘+๐œƒ๐‘˜
) + ๐‘ƒ๐‘’๐‘‘๐‘‘๐‘ฆ,๐‘๐‘ข ร— (
๐œƒโ„Ž๐‘ ,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘+๐œƒ๐‘˜
๐œƒโ„Ž๐‘ +๐œƒ๐‘˜
) (13)
The behavior of the eddy losses and DC losses are shown in Peddy and Pdc respectively. DC loss is
directly proportional to temperature, while eddy current loss is inversely proportional to temperature. ำจk is
the temperature coefficient of loss correction. Aluminum is equal to 225 and copper is equal to 235.Oil time
constant (ฯ„0) is one of the most important parameters that should be determined accurately. Note that, there
are specific methods for each thermal model to determine ฯ„0. The oil time constant for dynamic thermal
model is given by [20]: Note that, (14) is based on minute and (15) is per hours and depends on whether per
hours or minutes have to be changed and for data which collected per hours it shouldnโ€™t multiply by 60, it
means that the oil time constant does not need to convert to minutes.
๐œ0 =
๐ถ๐‘กโ„Žโˆ’๐‘œ๐‘–๐‘™ร—๐›ฅ๐œƒ๐‘œ๐‘–๐‘™,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘
๐‘ƒ๐‘ก๐‘œ๐‘ก๐‘Ž๐‘™
ร— 60 (14)
๐œ0 =
๐ถ๐‘กโ„Žโˆ’๐‘œ๐‘–๐‘™ร—๐›ฅ๐œƒ๐‘œ๐‘–๐‘™,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘
๐‘ƒ๐‘ก๐‘œ๐‘ก๐‘Ž๐‘™
(15)
3. RESEARCH METHOD
3.1. Solving techniques
3.1.1. IEEE standard method
IEEE standards C57.91-1995 has offered an exponential method based on the (14) to calculate the
TOT to determine the HST of transformers for classic thermal model [3]. In (14) is derived from (1) [21].
๐›ฅ๐œƒ๐‘‡๐‘‚ = (๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘ˆ โˆ’ ๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘–) [1 โˆ’ ๐‘’๐‘ฅ๐‘
โˆ’1
๐‘‡0] + ๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘– (16)
The ultimate value of top oil acsent for each stage is calculated by,
๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘ข = ๐œƒ๐‘“๐‘™ [
(๐ผ๐‘๐‘ข,๐‘ข
2 ๐‘…+1)
(๐‘…+1)
]
๐‘›
(17)
For calculating the initial value for the first time, t=0, knowing the record of loading profile can be
so useful. The current at t=0, determined by RMS value of the loading currents for the former loadings [3].
Equation (3.5) can be used to estimate the initial value for other steps to calculate the top-oil temperature rise.
๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘– = ๐œƒ๐‘“๐‘™ [
(๐ผ๐‘๐‘ข,๐‘–
2
๐‘…+1)
(๐‘…+1)
]
๐‘›
(18)
3.1.2. Numerical method
Numerical methods are used to solve the ordinary differential equation. In this study, two types of
numerical solvers are compared to determine the thermal-electrical models. The first model is related to
Bulletin of Electr Eng & Inf ISSN: 2302-9285 ๏ฒ
Analysis of thermal models to determine the loss of life of mineral oil โ€ฆ (Mohammad Tolou Askari)
2331
Euler's method and is the simplest solver. Although this model is not an appropriate solver in most
utilization, it reveals some common characteristics among different types of solvers. Runge-Kutta is the
second type of solver, which is used in this paper. The fourth-order RungeKutta technique is the most widely
used solution method. This solution technique, which begins with an initial value (t0,y0), has four slopes,
1 0 0
( , ),
K f t y
๏€ฝ ๐พ2 = ๐‘“(๐‘ก0 +
โ„Ž
2
, ๐‘ฆ0 +
โ„Ž
2
๐พ1),
3 0 0 2
( , ),
2 2
h h
K f t y K
๏€ฝ ๏€ซ ๏€ซ ๐พ4 = ๐‘“(๐‘ก0 + โ„Ž, ๐‘ฆ0 + โ„Ž๐พ3) (19)
With these slopes, the next value of the dependent variable can be determined as,
๐‘ฆ๐‘˜ = ๐‘ฆ๐‘˜โˆ’1 + โ„Ž
๐พ1+2๐พ2+2๐พ3+๐พ4
6
(20)
TOT and HST of transformer can be computed for dynamic thermal model according to the algorithm
has been given in Figure 2. The input data can be classified in two groups, constant and variable input data.
Constant data are n, m, weight of the oil per kg, load losses and no-load losses, oil time constant and winding
time constant, DC and eddy losses, And the hot spot temperature under rated load. While variable input data
that can be changed by time include current or loading of transformers and ambient temperature.
Figure 2. HST and TOT for dynamic thermal model
*: N is total number of load current that are collected
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3.2. The loss of life of the transformer
The quality of paper and oil which are applied in electrical transformer is directly proportional to the
efficiency of it. However, the deterioration of paper can determine the loss of life (LOL) the mineral oil
immersed transformers. Heat, oxygen and moisture are the most important factors to deteriorate the paper of
electrical transformers. Insulation degradation can be simulated as a quantity per unit and calculated as [4],
[22];
๐‘๐‘’๐‘Ÿ โˆ’ ๐‘ข๐‘›๐‘–๐‘ก โˆ’ ๐‘™๐‘–๐‘“๐‘’ = ๐ด๐‘’
[
๐ต
๐œƒ๐ป๐‘†๐‘‡+273
]
(21)
where: A=is an adjusted constant based on the temperature determined for a per unit life,
B=is the slope rate of aging.
IEEE standard C57.91-1995 considered B=15000 is appropriate and is used in per-unit-life equation
for loading of transformers. For ๐œƒ๐ป๐‘†๐‘‡=110 C, and per-unit-life=1, the value of A constant becomes
9.8ร—10-18. The aging factor can be calculated [3], [23]
๐น๐ด๐ด = ๐‘’
[
15000
383
โˆ’
15000
๐œƒ๐ป+273
]
(22)
The equivalent aging of the electrical transformer based on reference temperature for hottest spot
is 110ยฐ๐ถcould be calculated as [3], [24], [25]:
๐น๐ธ๐‘„๐ด =
โˆ‘ ๐น๐ด๐ด๐‘›๐›ฅ๐‘ก๐‘›
๐‘
๐‘›=1
โˆ‘ ๐›ฅ๐‘ก๐‘›
๐‘
๐‘›=1
(23)
where: FEQA=aging factor
n=time interval index
N=total time duration
๐›ฅ๐‘ก๐‘›=time interval
And, the percentage of LOL can be determined as [26], [27]:
%๐‘™๐‘œ๐‘ ๐‘  โˆ’ ๐‘œ๐‘“ โˆ’ ๐‘™๐‘–๐‘“๐‘’ =
๐น๐ธ๐‘„๐ดร—๐‘กร—100
๐‘๐ผ๐ฟ
(24)
3.3. Emprical tests for case of study
3.3.1. Three phase 2500 KVA transformer
The ratio of voltage of 2500 KVA transformer is 20/0.4 KV, and without external cooling, ONAN.
Three different loading currents are considered in this paper that are shown in Table 3. For this transformer
the low voltage and high voltage windings have one and two axial cooling duct respectively. The transformer
equipped by 17 thermocouples located as follows: One is mounted 50 mm under the tank cover of electrical
transformer, 2 sensors in the oil enclosure,4 sensors is located on the bottom of outside surface of the tank, 2
in the bottom of the tank, 4 in duct outlet in top and bottom, 4 in duct inlet in top and bottom.
Table 3. Load levels for transformer
Time intervals (minutes) Load (PU)
0-300 1
300-382 2
382-415 0
3.3.2. Three phase 30 MVA transformer
The voltage ratio of this transformer is 33/11 KV. Also, cooling system is oil natural and air force
(ONAF). 3 thermometers are used to indicate the winding and top oil temperatures for high and low voltage
windings. Also, they are used for collecting ambient temperature. This data is necessary to verify the
suggested techniques provided in this article. The output of the thermometer is a function of the 4 to 20 mA
current that must be converted to temperature (C).
4. RESULTS AND DISCUSSION
HST of each transformer has been plotted for both distribution transformers. LOL of transformers
for each thermal model has been compared with measured value and were indicated in Tables 4 and 7 for
Bulletin of Electr Eng & Inf ISSN: 2302-9285 ๏ฒ
Analysis of thermal models to determine the loss of life of mineral oil โ€ฆ (Mohammad Tolou Askari)
2333
classic thermal model and Tables 5 and 8 for dynamic thermal model. Finally, Tables 6, and 9 tabulate the
error of numerical methods rather than exponential method. By comparing the error of each thermal model
for 2500 KVA transformer, which is demonstrated in Tables 4 and 5, the less error of dynamic thermal model
rather than classic thermal model is comprehensible. These errors for numerical methods are less than
exponential method.
4.1. 2500 KVA transformer
2500 KVA transformer was tested for 415 minutes. Figure 3 shows the comparison between the
measured HST and HST achieved by the numerical methods and exponential method. Graphs have been
plotted based on the classic model. Figure 4 shows the comparison of the hot spot temperature of a 2500
KVA transformer with the hot spot temperature calculated using two numerical methods (RungeKutta and
Euler methods).This graph has been plotted based on the dynamic thermal model.
Figure 3. Hot spot temperature of 2500 KVA transformer: Classic thermal model
Figure 4. Hot spot temperature of 2500 KVA transformer: Dynamic thermal model
In Tables 4 and 5 show the comparison between the errors achieved for classis and dynamic thermal
models respectively. These errors given the differences between the numerical methods and exponential
methods with measured. In addition, the loss of life of the 2500 KVA transformer is compared with measured
0 50 100 150 200 250 300 350 400 450
20
40
60
80
100
120
140
160
180
200
220
HST for 2500kVA Irantranfo transformer
Time (min)
Temperature
(C)
Proposed method
Euler
Measured
Exponential
0 50 100 150 200 250 300 350 400 450
20
40
60
80
100
120
140
160
180
200
220
Time(min)
Temperature(C)
HST for 2500KVA transformer
Proposed Model
Euler
measured
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value in the Table 6 for two types of the thermal models. Thermal models have been calculated based on R-K
technique. This comparison shows that the accuracy of the dynamic thermal model is higher than that of the
classical thermal model.
Table 4. Classic thermal model of 2500 KVA transformer (ERROR OF LOL)
Error for RK4 |(๐ฟ๐‘‚๐ฟ๐‘๐‘ˆ๐‘€ โˆ’ ๐ฟ๐‘‚๐ฟ๐‘€๐‘’๐‘Ž๐‘ ๐‘ข๐‘Ÿ๐‘’๐‘‘)| Error of exponential|(๐ฟ๐‘‚๐ฟ๐ผ๐ธ๐ธ๐ธ โˆ’ ๐ฟ๐‘‚๐ฟ๐‘€๐‘’๐‘Ž๐‘ ๐‘ข๐‘Ÿ๐‘’๐‘‘)|
1.7052 2.7643
Table 5. Dynamic thermal model of 2500 KVA transformer (ERROR OF LOL)
Error for RK4 method |(๐‘™๐‘œ๐‘™๐‘…๐พ4 โˆ’ ๐‘™๐‘œ๐‘™๐‘€๐‘’๐‘Ž๐‘ ๐‘ข๐‘Ÿ๐‘’๐‘‘)| Error for Euler method |(๐‘™๐‘œ๐‘™๐ธ๐‘ข๐‘™๐‘’๐‘Ÿ โˆ’ ๐‘™๐‘œ๐‘™๐‘€๐‘’๐‘Ž๐‘ ๐‘ข๐‘Ÿ๐‘’๐‘‘)|
0.7806 1.4912
Table 6. Error of thermal models: Different solving technique
numerical technique
(Dynamic thermal model )
numerical technique
(Classic thermal model)
exponential technique
(Classic thermal model)
0.2358 2.2503 2.7643
5. CONCLUSION
Several thermal models and solution are suggested for solving various thermal models to calculate
the TOT and HST of transformer due to loss of life evaluation. These methods involved are linear and
nonlinear regression and exponential methods that are proposed by IEEE standard. Numerical methods can
be used as solution to calculate the thermal model, R-K technique is an improved numerical method proposed
in this research for solving two types of thermal models the first one is classical thermal model that was
suggested by IEEE standard C57.91-1995 and the second one is thermal-electrical model or dynamic thermal
model that assumed number of variable parameters such as viscosity of oil, ambient temperature, eddy losses.
According to the results the proposed technique for solving the thermal models shows improved accuracy
over the traditional methods.
ACKNOWLEDGEMENTS
The authors of this paper would like to appreciate Universiti Tenaga Nasional (UNITEN), Malaysia,
for funding this publication through BOLD 2025 research grant (RJO10517844/071).
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๏ฒ ISSN: 2302-9285
Bulletin of Electr Eng & Inf, Vol. 10, No. 5, October 2021 : 2327 โ€“ 2336
2336
BIOGRAPHIES OF AUTHORS
Mohammad Tolou Askari received his Bachelor degree in Power Electrical Engineering
from University of Applied Science and Technology of Mashhad in 2005, and the Master
degree in Power Electrical Engineering in 2008. He received Ph.D. degree in Power Electrical
Engineering from University Putra Malaysia in 2004. Currently, he is a senior lecturer in the
Department of Electrical and Electronics Engineering, Faculty of Engineering, Islamic Azad
Universityโ€
Mohammadi M. Javad received the B.Eng degree in Electrical in 2018 and master of power
system engineering from Islamic Azad university of Semnan.his research interests include
comparison thermal model and numerical solution methods estimate Insulation life of
electrical transformers power system engineering from Islamic Azad university of Semnan.
Dr. Jagadeesh Pasupuleti is the Head of Hybrid Renewable Energy Systems, Institute of
Sustainable Energy, Universiti Tenaga Nasional, Malaysia. He is a Senior Member of IEEE
(USA), Member of IET (UK), Chartered Engineer (UK), Professional Review Interviewer for
CEng (UK), Member of EI (UK), Member of BEM (Malaysia) and Member of ISTE (India).
He has supervised 30 postgraduate students, published over 100 papers and involved in 50
research and consultancy projects funded around $ 3 million in renewable energy.
Mehrdad Tahmasebi received his Bachelor degree in Power Electrical Engineering from
Islamic Azad University, South Tehran branch, Iran in 2002, and the Master degree in Power
Electrical Engineering&Electrical Energy Management from Amirkabir University of
Technology, Tehran, Iran in 2010. He received Ph.D. degree in Power Electrical Engineering
from The National Energy University of Malaysia in 2015. Currently, he is an Assistant
Professor in the Department of Electrical Engineering, Islamic Azad University (Ilam
Branch).โ€
Shangari K. Raveendran received the B. Eng degree in Electrical and Electronic in 2009 and
Masters in Electrical Engineering in 2011 Engineering from Universiti Tenaga Nasional.
Currently, she is a lecturer in the Department of Electrical and Electronics Engineering,
College of Engineering, Universiti Tenaga Nasional. Her research interests includes power
system, renewable energy, virtual power plant, energy management system and battery storage
system.โ€
Mohd. Zainal Abidin Ab. Kadir received the B. Eng degree in Electrical and Electronic
Engineering from Universiti Putra Malaysia in 2000 and Ph.D. degree in High Voltage
Engineering from The Universiti of Manchester in UK in 2006. Currently, he is a professor in
the Department of Electrical and Electronics Engineering, Faculty of Engineering, University
Putra Malaysia. โ€œ

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Analysis of thermal models to determine the loss of life of mineral oil immersed transformers

  • 1. Bulletin of Electrical Engineering and Informatics Vol. 10, No. 5, October 2021, pp. 2327~2336 ISSN: 2302-9285, DOI: 10.11591/eei.v10i5.3131 ๏ฒ2327 Journal homepage: http://beei.org Analysis of thermal models to determine the loss of life of mineral oil immersed transformers Mohammad Tolou Askari1 , Mohammad Javad Mohammadi2 , Jagadeesh Pasupuleti3 , Mehrdad Tahmasebi4 , Shangari K Raveendran5 , Mohd Zainal Abdin Ab Kadir6 1,2 Department of Electrical Engineering, Semnan Branch, Islamic Azad University, Semnan, Iran 3,5 Institute of Sustainable Energy, Universiti Tenaga Nasional (UNITEN), Kajang, Malaysia 4 Department of Electrical Engineering, Ilam Branch, Islamic Azad University, Ilam, Iran 6 Institute of Power Engineering (IPE), Universiti Tenaga Nasional (UNITEN), Kajang, Malaysia 6 Centre for Electromagnetic and Lightning Protection Research (CELP), Faculty of Engineering, Universiti Putra Malaysia, Serdang, Malaysia Article Info ABSTRACT Article history: Received Dec 2, 2019 Revised May 2, 2021 Accepted Jul 14, 2021 Hot spot as well as top oil temperatures have played the most effective parameters on the life of the electrical transformers. The prognostication of these factors is very vital for determining the residual life of the electrical transformers in the transmission and distribution systems. Thus, an accurate mathematical method is required to calculate the critical temperature such as hot spot and top oil temperature based on the different types of thermal models. In this study calculates the service life of the transformers based on an accurate top oil temperature. Accordingly, An approach solution is given for calculating the thermal model. Also, findings are validated with true temperatures. Finally, this method is implemented on 2500 KVA electrical transformer. Keywords: Electrical transformer Hot spot temprature Numerical analysis Thermal model This is an open access article under the CC BY-SA license. Corresponding Author: Mohammad Tolou Askari Department of Electrical Engineering, Semnan Branch Islamic Azad University, Semnan, Iran Email: m.askari@semnaniau.ac.ir 1. INTRODUCTION Electrical transformers the facilities in electrical power networks that the correct operation of it has played main role in providing reliability of these systems. By noticing the costs of transformers and permanent connection of transformers to transmission and distribution systems, any action to increase the life cause improvement in the operation of power systems. Life of the electrical transformer and loading capabilities of this facilities depend on several parameters. Oil and paper in transformers are two insulation materials, that the integrity of them warranties the life of transformers. Hot spot temperature (HST) and top oil temperature (TOT) are two criteria to evaluate the integrity of these two insulation materials and transformers as important facility in power network [1]-[3]. These criteria determine the temperature limitation of transformer for loading capability, for example the IEEE standard suggests that the TOT rise over ambient temperature 65ยฐC and depending on it has considered 110ยฐC for HST [4]-[6]. It means that increasing the temperature of transformer over this standard value causes the degradation of insulation life of transformer. According to research, from 90ยฐC to 110ยฐC, the aging rate of tensile strength approximately doubles every 5ยฐC to 10ยฐC temperature rise [2], [3], [7]-[9]. A. A. Taheri, A. Abdali and A. Rabiee [10] a thermal resistance with solar radiation is used to explain the heat transfer theory in transformer. The effect of
  • 2. ๏ฒ ISSN: 2302-9285 Bulletin of Electr Eng & Inf, Vol. 10, No. 5, October 2021 : 2327 โ€“ 2336 2328 long term ambient temperature was investigated in [11], [12]. There are some dynamic factors in oil immersed transformer such as ambient temperatures, winding losses and oil viscosity of transformer [3], [13]. In this article, two thermal models, classic thermal model as famous and reliable thermal model and dynamic thermal model as improved thermal model, has been used. Moreover, TOT and HST is calculated for both thermal model by IEEE standard method that has been available in [3] and also these temperatures are calculated by proposed method. To validate and show the tolerance of numerical technique, the results of models compared with measured value. 2. LITERATURE REVIEW 2.1. Thermal model 2.1.1. Classic thermal model Thermal model is used to estimate the critical temperature of the transformer. The classic one was given base on the heat generated and distributed in the windings and oil of transformer [3], [9]. Figure 1 shows temperature distribution in the transformer. Figure 1. The temperature distribution in the transformer The classic thermal model is used by a differential equation as [3]: ๐‘‡0 ๐‘‘๐œƒ๐‘ก๐‘œ๐‘ ๐‘‘๐‘ก = โˆ’๐œƒ๐‘ก๐‘œ๐‘ + ๐œƒ๐‘ข + ๐œƒ๐‘Ž๐‘š๐‘ (1) The solution as: ๐œƒ๐‘ก๐‘œ๐‘ = (๐œƒ๐‘ข + ๐œƒ๐‘Ž๐‘š๐‘ โˆ’ ๐œƒ๐‘ก๐‘œ๐‘๐‘–)(1 โˆ’ ๐‘’ โˆ’( ๐‘ก ๐‘‡0 ) ) + ๐œƒ๐‘ก๐‘œ๐‘๐‘–โ€ (2) and ๐œƒ๐‘ข = ๐œƒ๐‘“๐‘™ [ ๐ผ๐‘๐‘ข 2 ๐‘…+1 ๐‘…+1 ] ๐‘› (3) ๐‘‡0 = ๐ถ๐œƒ๐‘“๐‘™ ๐‘ƒ๐‘“๐‘™ (4) where: ๐œƒ๐‘‡๐‘‚๐‘ƒ=Top-oil rise over ambient temperature (C) ๐œƒ๐‘ข=Ultimate top-oil rise for load L (C) ๐œƒ๐‘–=Initial top-oil rise for t=0 (C) ๐œƒ๐‘“๐‘™=Top-oil rise over ambient temperature at rated load ๐‘‡0=Time constant ๐‘›=Oil exponent
  • 3. Bulletin of Electr Eng & Inf ISSN: 2302-9285 ๏ฒ Analysis of thermal models to determine the loss of life of mineral oil โ€ฆ (Mohammad Tolou Askari) 2329 ๐ผ=Specified load ๐ผ๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘=Rated load ๐ผ๐‘๐‘ข=Ratio of specified load to rated load The transient rise of the hottest spot of the winding higher than the upper limit of the oil temperature is determined by the following formula [3]: ๐›ฅ๐œƒ๐ป = (๐›ฅ๐œƒ๐ป,๐‘ˆ โˆ’ ๐›ฅ๐œƒ๐ป,๐‘–) [1 โˆ’ ๐‘’๐‘ฅ๐‘ โˆ’๐‘ก ๐‘‡0 ] + ๐›ฅ๐œƒ๐ป,๐‘– (5) That the initial value for hot-spot temperature rise over top-oil temperature is given by: ๐›ฅ๐œƒ๐ป,๐‘– = ๐›ฅ๐œƒ๐ป,๐‘…๐ผ๐‘–,๐‘๐‘ข 2๐‘š (6) The maximum hot spots are as follows: ๐›ฅ๐œƒ๐ป,๐‘ˆ = ๐›ฅ๐œƒ๐ป,๐‘…๐ผ๐‘ˆ,๐‘๐‘ข 2๐‘š (7) The nominal hottest temperature spot value is given by: ๐›ฅ๐œƒ๐ป,๐‘… = ๐›ฅ๐œƒ๐ป/๐ด,๐‘… โˆ’ ๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘… (8) where: ๐›ฅ๐œƒ๐ป=Hottest temperature spot rise over top oil temperature (C) ๐›ฅ๐œƒ๐ป,๐‘ˆ=Maximum hottest temperature spot rise over maximum oil temperature for load(C) ๐›ฅ๐œƒ๐ป,๐‘–=Initial hottest temperature spot rise over top oil temperature for t = 0 (C) ๐‘‡0=time constant of the transformer winding (h) ๐‘ก=Loading time (h) ๐›ฅ๐œƒ๐ป,๐‘…=Nominal hot spot rising above maximum oil temperature (C) ๐ผ=Current of load per unit M=The exponent determines the non-linearity as shown in Table 1 The manufacturer has specified the amount of n for each mode of cooling. The amounts of n and m for each cooling method are shown in Table 1 [3]. Table 1. Exponents for temperature determination formulas cooling M N OA 0.8 0.8 FA 0.8 0.9 Non-directed FOA or FOW 0.8 0.9 Directed FOA or FOW 1 1 HST will be calculated by (9). ๐œƒ๐ป๐‘†๐‘‡ = ๐›ฅ๐œƒ๐‘‡๐‘‚๐‘‡ + ๐›ฅ๐œƒ๐ป๐‘†๐‘‡ + ๐œƒ๐‘Ž๐‘š๐‘ (9) 2.2.2. Dynamic thermal model Firstly, A dynamic thermal model of electrical transformer has been offered by Swift based on the principals of heat transfer theory [14]-[17] after that an improved model has been introduced by Susa by assuming the non-linear thermal oil resistance base on swiftโ€™s approach. In Susaโ€™s model the variations of viscosity with temperature were considered [9]. TOT of dynamic thermal model is governed by (1). 1+๐‘…ร—๐พ2 1+๐‘… ร— ๐œ‡๐‘๐‘ข ๐‘› ร— ๐œƒ๐‘“๐‘™ = ๐œ‡๐‘๐‘ข ๐‘› ร— ๐œ0 ร— ๐‘‘๐œƒ๐‘œ๐‘–๐‘™ ๐‘‘๐‘ก + (๐œƒ๐‘œ๐‘–๐‘™โˆ’๐œƒ๐‘Ž๐‘š๐‘)1+๐‘› ๐œƒ๐‘“๐‘™ ๐‘› (10) Oil viscosity is added as a parameter. This can be determined by [18]. ๐œ‡๐‘๐‘ข = ๐‘’ [( 2797.3 ๐œƒ๐‘ก๐‘œ๐‘+273 )โˆ’( 2797.3 ๐œƒ๐‘“๐‘™+273 )] (11) where: ๐พ=load current per unit ๐‘…=proportionality of load to no-load losses ๐œ0=top oil time constant, (min) ๐œƒ๐‘“๐‘™=rated top oil rise over ambient, (K)
  • 4. ๏ฒ ISSN: 2302-9285 Bulletin of Electr Eng & Inf, Vol. 10, No. 5, October 2021 : 2327 โ€“ 2336 2330 ๐œƒ๐‘œ๐‘–๐‘™=top oil temperature gradient, (K) ๐œƒ๐‘Ž๐‘š๐‘=ambient temperature, (K) ๐œ‡๐‘๐‘ข=oil viscosity per unit ๐‘›=empirical constant, the amount of n has been specified for each cooling mode in Table 2 [2]. Tabel 2. Experimental value of n Oil circulation n With cooling without cooling Initial oil circulation, Speed=0, (cold start) ONAF/OFAF ONAN ONAN 0.5 0 0.25 โ€œInitial oil circulation, Speed>0, (transformer on load)โ€ 0.2 0.25 0.25 HST of dynamic thermal model is given as [19]: [๐พ2 ร— ๐‘ƒ๐‘ค๐‘‘,๐‘๐‘ข] ร— ๐œ‡๐‘๐‘ข ๐‘› ร— ๐›ฅ๐œƒโ„Ž๐‘ ,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘ = ๐œ‡๐‘๐‘ข ๐‘› ร— ๐œ๐‘ค๐‘‘,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘ ร— ๐‘‘๐œƒโ„Ž๐‘  ๐‘‘๐‘ก + ( (๐œƒโ„Ž๐‘ โˆ’๐œƒ๐‘œ๐‘–๐‘™)๐‘›+1 ๐›ฅ๐œƒโ„Ž๐‘ ,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘ ๐‘› ) (12) Pwd,pu, is the load lossโ€™s dependence on temperature that can be determined by (13) ๐‘ƒ๐‘ค๐‘‘,๐‘๐‘ข = ๐‘ƒ๐‘‘๐‘,๐‘๐‘ข ร— ( ๐œƒโ„Ž๐‘ +๐œƒ๐‘˜ ๐œƒโ„Ž๐‘ ,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘+๐œƒ๐‘˜ ) + ๐‘ƒ๐‘’๐‘‘๐‘‘๐‘ฆ,๐‘๐‘ข ร— ( ๐œƒโ„Ž๐‘ ,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘+๐œƒ๐‘˜ ๐œƒโ„Ž๐‘ +๐œƒ๐‘˜ ) (13) The behavior of the eddy losses and DC losses are shown in Peddy and Pdc respectively. DC loss is directly proportional to temperature, while eddy current loss is inversely proportional to temperature. ำจk is the temperature coefficient of loss correction. Aluminum is equal to 225 and copper is equal to 235.Oil time constant (ฯ„0) is one of the most important parameters that should be determined accurately. Note that, there are specific methods for each thermal model to determine ฯ„0. The oil time constant for dynamic thermal model is given by [20]: Note that, (14) is based on minute and (15) is per hours and depends on whether per hours or minutes have to be changed and for data which collected per hours it shouldnโ€™t multiply by 60, it means that the oil time constant does not need to convert to minutes. ๐œ0 = ๐ถ๐‘กโ„Žโˆ’๐‘œ๐‘–๐‘™ร—๐›ฅ๐œƒ๐‘œ๐‘–๐‘™,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘ ๐‘ƒ๐‘ก๐‘œ๐‘ก๐‘Ž๐‘™ ร— 60 (14) ๐œ0 = ๐ถ๐‘กโ„Žโˆ’๐‘œ๐‘–๐‘™ร—๐›ฅ๐œƒ๐‘œ๐‘–๐‘™,๐‘Ÿ๐‘Ž๐‘ก๐‘’๐‘‘ ๐‘ƒ๐‘ก๐‘œ๐‘ก๐‘Ž๐‘™ (15) 3. RESEARCH METHOD 3.1. Solving techniques 3.1.1. IEEE standard method IEEE standards C57.91-1995 has offered an exponential method based on the (14) to calculate the TOT to determine the HST of transformers for classic thermal model [3]. In (14) is derived from (1) [21]. ๐›ฅ๐œƒ๐‘‡๐‘‚ = (๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘ˆ โˆ’ ๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘–) [1 โˆ’ ๐‘’๐‘ฅ๐‘ โˆ’1 ๐‘‡0] + ๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘– (16) The ultimate value of top oil acsent for each stage is calculated by, ๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘ข = ๐œƒ๐‘“๐‘™ [ (๐ผ๐‘๐‘ข,๐‘ข 2 ๐‘…+1) (๐‘…+1) ] ๐‘› (17) For calculating the initial value for the first time, t=0, knowing the record of loading profile can be so useful. The current at t=0, determined by RMS value of the loading currents for the former loadings [3]. Equation (3.5) can be used to estimate the initial value for other steps to calculate the top-oil temperature rise. ๐›ฅ๐œƒ๐‘‡๐‘‚,๐‘– = ๐œƒ๐‘“๐‘™ [ (๐ผ๐‘๐‘ข,๐‘– 2 ๐‘…+1) (๐‘…+1) ] ๐‘› (18) 3.1.2. Numerical method Numerical methods are used to solve the ordinary differential equation. In this study, two types of numerical solvers are compared to determine the thermal-electrical models. The first model is related to
  • 5. Bulletin of Electr Eng & Inf ISSN: 2302-9285 ๏ฒ Analysis of thermal models to determine the loss of life of mineral oil โ€ฆ (Mohammad Tolou Askari) 2331 Euler's method and is the simplest solver. Although this model is not an appropriate solver in most utilization, it reveals some common characteristics among different types of solvers. Runge-Kutta is the second type of solver, which is used in this paper. The fourth-order RungeKutta technique is the most widely used solution method. This solution technique, which begins with an initial value (t0,y0), has four slopes, 1 0 0 ( , ), K f t y ๏€ฝ ๐พ2 = ๐‘“(๐‘ก0 + โ„Ž 2 , ๐‘ฆ0 + โ„Ž 2 ๐พ1), 3 0 0 2 ( , ), 2 2 h h K f t y K ๏€ฝ ๏€ซ ๏€ซ ๐พ4 = ๐‘“(๐‘ก0 + โ„Ž, ๐‘ฆ0 + โ„Ž๐พ3) (19) With these slopes, the next value of the dependent variable can be determined as, ๐‘ฆ๐‘˜ = ๐‘ฆ๐‘˜โˆ’1 + โ„Ž ๐พ1+2๐พ2+2๐พ3+๐พ4 6 (20) TOT and HST of transformer can be computed for dynamic thermal model according to the algorithm has been given in Figure 2. The input data can be classified in two groups, constant and variable input data. Constant data are n, m, weight of the oil per kg, load losses and no-load losses, oil time constant and winding time constant, DC and eddy losses, And the hot spot temperature under rated load. While variable input data that can be changed by time include current or loading of transformers and ambient temperature. Figure 2. HST and TOT for dynamic thermal model *: N is total number of load current that are collected
  • 6. ๏ฒ ISSN: 2302-9285 Bulletin of Electr Eng & Inf, Vol. 10, No. 5, October 2021 : 2327 โ€“ 2336 2332 3.2. The loss of life of the transformer The quality of paper and oil which are applied in electrical transformer is directly proportional to the efficiency of it. However, the deterioration of paper can determine the loss of life (LOL) the mineral oil immersed transformers. Heat, oxygen and moisture are the most important factors to deteriorate the paper of electrical transformers. Insulation degradation can be simulated as a quantity per unit and calculated as [4], [22]; ๐‘๐‘’๐‘Ÿ โˆ’ ๐‘ข๐‘›๐‘–๐‘ก โˆ’ ๐‘™๐‘–๐‘“๐‘’ = ๐ด๐‘’ [ ๐ต ๐œƒ๐ป๐‘†๐‘‡+273 ] (21) where: A=is an adjusted constant based on the temperature determined for a per unit life, B=is the slope rate of aging. IEEE standard C57.91-1995 considered B=15000 is appropriate and is used in per-unit-life equation for loading of transformers. For ๐œƒ๐ป๐‘†๐‘‡=110 C, and per-unit-life=1, the value of A constant becomes 9.8ร—10-18. The aging factor can be calculated [3], [23] ๐น๐ด๐ด = ๐‘’ [ 15000 383 โˆ’ 15000 ๐œƒ๐ป+273 ] (22) The equivalent aging of the electrical transformer based on reference temperature for hottest spot is 110ยฐ๐ถcould be calculated as [3], [24], [25]: ๐น๐ธ๐‘„๐ด = โˆ‘ ๐น๐ด๐ด๐‘›๐›ฅ๐‘ก๐‘› ๐‘ ๐‘›=1 โˆ‘ ๐›ฅ๐‘ก๐‘› ๐‘ ๐‘›=1 (23) where: FEQA=aging factor n=time interval index N=total time duration ๐›ฅ๐‘ก๐‘›=time interval And, the percentage of LOL can be determined as [26], [27]: %๐‘™๐‘œ๐‘ ๐‘  โˆ’ ๐‘œ๐‘“ โˆ’ ๐‘™๐‘–๐‘“๐‘’ = ๐น๐ธ๐‘„๐ดร—๐‘กร—100 ๐‘๐ผ๐ฟ (24) 3.3. Emprical tests for case of study 3.3.1. Three phase 2500 KVA transformer The ratio of voltage of 2500 KVA transformer is 20/0.4 KV, and without external cooling, ONAN. Three different loading currents are considered in this paper that are shown in Table 3. For this transformer the low voltage and high voltage windings have one and two axial cooling duct respectively. The transformer equipped by 17 thermocouples located as follows: One is mounted 50 mm under the tank cover of electrical transformer, 2 sensors in the oil enclosure,4 sensors is located on the bottom of outside surface of the tank, 2 in the bottom of the tank, 4 in duct outlet in top and bottom, 4 in duct inlet in top and bottom. Table 3. Load levels for transformer Time intervals (minutes) Load (PU) 0-300 1 300-382 2 382-415 0 3.3.2. Three phase 30 MVA transformer The voltage ratio of this transformer is 33/11 KV. Also, cooling system is oil natural and air force (ONAF). 3 thermometers are used to indicate the winding and top oil temperatures for high and low voltage windings. Also, they are used for collecting ambient temperature. This data is necessary to verify the suggested techniques provided in this article. The output of the thermometer is a function of the 4 to 20 mA current that must be converted to temperature (C). 4. RESULTS AND DISCUSSION HST of each transformer has been plotted for both distribution transformers. LOL of transformers for each thermal model has been compared with measured value and were indicated in Tables 4 and 7 for
  • 7. Bulletin of Electr Eng & Inf ISSN: 2302-9285 ๏ฒ Analysis of thermal models to determine the loss of life of mineral oil โ€ฆ (Mohammad Tolou Askari) 2333 classic thermal model and Tables 5 and 8 for dynamic thermal model. Finally, Tables 6, and 9 tabulate the error of numerical methods rather than exponential method. By comparing the error of each thermal model for 2500 KVA transformer, which is demonstrated in Tables 4 and 5, the less error of dynamic thermal model rather than classic thermal model is comprehensible. These errors for numerical methods are less than exponential method. 4.1. 2500 KVA transformer 2500 KVA transformer was tested for 415 minutes. Figure 3 shows the comparison between the measured HST and HST achieved by the numerical methods and exponential method. Graphs have been plotted based on the classic model. Figure 4 shows the comparison of the hot spot temperature of a 2500 KVA transformer with the hot spot temperature calculated using two numerical methods (RungeKutta and Euler methods).This graph has been plotted based on the dynamic thermal model. Figure 3. Hot spot temperature of 2500 KVA transformer: Classic thermal model Figure 4. Hot spot temperature of 2500 KVA transformer: Dynamic thermal model In Tables 4 and 5 show the comparison between the errors achieved for classis and dynamic thermal models respectively. These errors given the differences between the numerical methods and exponential methods with measured. In addition, the loss of life of the 2500 KVA transformer is compared with measured 0 50 100 150 200 250 300 350 400 450 20 40 60 80 100 120 140 160 180 200 220 HST for 2500kVA Irantranfo transformer Time (min) Temperature (C) Proposed method Euler Measured Exponential 0 50 100 150 200 250 300 350 400 450 20 40 60 80 100 120 140 160 180 200 220 Time(min) Temperature(C) HST for 2500KVA transformer Proposed Model Euler measured
  • 8. ๏ฒ ISSN: 2302-9285 Bulletin of Electr Eng & Inf, Vol. 10, No. 5, October 2021 : 2327 โ€“ 2336 2334 value in the Table 6 for two types of the thermal models. Thermal models have been calculated based on R-K technique. This comparison shows that the accuracy of the dynamic thermal model is higher than that of the classical thermal model. Table 4. Classic thermal model of 2500 KVA transformer (ERROR OF LOL) Error for RK4 |(๐ฟ๐‘‚๐ฟ๐‘๐‘ˆ๐‘€ โˆ’ ๐ฟ๐‘‚๐ฟ๐‘€๐‘’๐‘Ž๐‘ ๐‘ข๐‘Ÿ๐‘’๐‘‘)| Error of exponential|(๐ฟ๐‘‚๐ฟ๐ผ๐ธ๐ธ๐ธ โˆ’ ๐ฟ๐‘‚๐ฟ๐‘€๐‘’๐‘Ž๐‘ ๐‘ข๐‘Ÿ๐‘’๐‘‘)| 1.7052 2.7643 Table 5. Dynamic thermal model of 2500 KVA transformer (ERROR OF LOL) Error for RK4 method |(๐‘™๐‘œ๐‘™๐‘…๐พ4 โˆ’ ๐‘™๐‘œ๐‘™๐‘€๐‘’๐‘Ž๐‘ ๐‘ข๐‘Ÿ๐‘’๐‘‘)| Error for Euler method |(๐‘™๐‘œ๐‘™๐ธ๐‘ข๐‘™๐‘’๐‘Ÿ โˆ’ ๐‘™๐‘œ๐‘™๐‘€๐‘’๐‘Ž๐‘ ๐‘ข๐‘Ÿ๐‘’๐‘‘)| 0.7806 1.4912 Table 6. Error of thermal models: Different solving technique numerical technique (Dynamic thermal model ) numerical technique (Classic thermal model) exponential technique (Classic thermal model) 0.2358 2.2503 2.7643 5. CONCLUSION Several thermal models and solution are suggested for solving various thermal models to calculate the TOT and HST of transformer due to loss of life evaluation. These methods involved are linear and nonlinear regression and exponential methods that are proposed by IEEE standard. Numerical methods can be used as solution to calculate the thermal model, R-K technique is an improved numerical method proposed in this research for solving two types of thermal models the first one is classical thermal model that was suggested by IEEE standard C57.91-1995 and the second one is thermal-electrical model or dynamic thermal model that assumed number of variable parameters such as viscosity of oil, ambient temperature, eddy losses. According to the results the proposed technique for solving the thermal models shows improved accuracy over the traditional methods. ACKNOWLEDGEMENTS The authors of this paper would like to appreciate Universiti Tenaga Nasional (UNITEN), Malaysia, for funding this publication through BOLD 2025 research grant (RJO10517844/071). REFERENCES [1] M. Djamali and S. Tenbohlen, "Hundred years of experience in the dynamic thermal modelling of power transformers," IET Generation, Transmission & Distribution, vol. 11, pp. 2731-2739, 2017. [2] H. Nafisi, "Investigation on distribution transformer loss-of-life due to plug-in hybrid electric vehicles charging," International Journal of Ambient Energy, vol. 42, pp. 744-750, 2021, doi: 10.1080/01430750.2018.1563816. [3] IEEE, ""Guide for Loading Mineral-Oil-Immersed Power Transformers" C57.91-1995.," ed, 1995. [4] C.-c. Sun, C. Xiao, J. Hou, L. Kong, J. Ye, and W.-j. Yu, "Analysis of Factors Affecting Temperature Rise of Oil- immersed Power Transformer," in Journal of Physics: Conference Series, 2020, p. 012087, doi:10.1088/1742- 6596/1639/1/012087. [5] J. I. Aizpurua, S. D. J. McArthur, B. G. Stewart, B. Lambert, J. G. Cross and V. M. Catterson, "Adaptive Power Transformer Lifetime Predictions Through Machine Learning and Uncertainty Modeling in Nuclear Power Plants," in IEEE Transactions on Industrial Electronics, vol. 66, no. 6, pp. 4726-4737, June 2019, doi: 10.1109/TIE.2018.2860532. [6] V. Bissuel et al., "Novel Approach to the Extraction of Delphi-like Boundary-Condition-Independent Compact Thermal Models of Planar Transformer Devices," 2018 24rd International Workshop on Thermal Investigations of ICs and Systems (THERMINIC), 2018, pp. 1-7, doi: 10.1109/THERMINIC.2018.8593283. [7] B. C. Lesieutre, W. H. Hagman and J. L. Kirtley, "An improved transformer top oil temperature model for use in an on-line monitoring and diagnostic system," in IEEE Transactions on Power Delivery, vol. 12, no. 1, pp. 249-256, Jan. 1997, doi: 10.1109/61.568247. [8] L. W. Pierce, "Predicting liquid filled transformer loading capability," [1992] Record of Conference Papers Industry Applications Society 39th Annual Petroleum and Chemical Industry Conference, 1992, pp. 197-207, doi: 10.1109/PCICON.1992.229310.
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  • 10. ๏ฒ ISSN: 2302-9285 Bulletin of Electr Eng & Inf, Vol. 10, No. 5, October 2021 : 2327 โ€“ 2336 2336 BIOGRAPHIES OF AUTHORS Mohammad Tolou Askari received his Bachelor degree in Power Electrical Engineering from University of Applied Science and Technology of Mashhad in 2005, and the Master degree in Power Electrical Engineering in 2008. He received Ph.D. degree in Power Electrical Engineering from University Putra Malaysia in 2004. Currently, he is a senior lecturer in the Department of Electrical and Electronics Engineering, Faculty of Engineering, Islamic Azad Universityโ€ Mohammadi M. Javad received the B.Eng degree in Electrical in 2018 and master of power system engineering from Islamic Azad university of Semnan.his research interests include comparison thermal model and numerical solution methods estimate Insulation life of electrical transformers power system engineering from Islamic Azad university of Semnan. Dr. Jagadeesh Pasupuleti is the Head of Hybrid Renewable Energy Systems, Institute of Sustainable Energy, Universiti Tenaga Nasional, Malaysia. He is a Senior Member of IEEE (USA), Member of IET (UK), Chartered Engineer (UK), Professional Review Interviewer for CEng (UK), Member of EI (UK), Member of BEM (Malaysia) and Member of ISTE (India). He has supervised 30 postgraduate students, published over 100 papers and involved in 50 research and consultancy projects funded around $ 3 million in renewable energy. Mehrdad Tahmasebi received his Bachelor degree in Power Electrical Engineering from Islamic Azad University, South Tehran branch, Iran in 2002, and the Master degree in Power Electrical Engineering&Electrical Energy Management from Amirkabir University of Technology, Tehran, Iran in 2010. He received Ph.D. degree in Power Electrical Engineering from The National Energy University of Malaysia in 2015. Currently, he is an Assistant Professor in the Department of Electrical Engineering, Islamic Azad University (Ilam Branch).โ€ Shangari K. Raveendran received the B. Eng degree in Electrical and Electronic in 2009 and Masters in Electrical Engineering in 2011 Engineering from Universiti Tenaga Nasional. Currently, she is a lecturer in the Department of Electrical and Electronics Engineering, College of Engineering, Universiti Tenaga Nasional. Her research interests includes power system, renewable energy, virtual power plant, energy management system and battery storage system.โ€ Mohd. Zainal Abidin Ab. Kadir received the B. Eng degree in Electrical and Electronic Engineering from Universiti Putra Malaysia in 2000 and Ph.D. degree in High Voltage Engineering from The Universiti of Manchester in UK in 2006. Currently, he is a professor in the Department of Electrical and Electronics Engineering, Faculty of Engineering, University Putra Malaysia. โ€œ