UDK 620.194.22
DOI: 10.15587/2313-8416.2019.179545
SUSCEPTIBILITY OF PIPE STEEL OF A CONTROLLABLE ROLLING TO STRESS-CORROSION CRACKING
L. Nyrkova, A. Rybakov, S. Melnychuk, S. Osadchuk
До^джено схильтсть трубног cmani Х70 до корозтного розтрiскування eid напруження (КРН) в умо-вах комплексного впливу чинниюв. Чутливiсть до КРН оцiнювали за коефщентом Ks (спiввiдношення ei-дносного звуження зразка у повiтрi до його вiдносного звуження у розчит). Сприйнятливкть сталi X70 до КРН при потенцiалi корози - низька, але збыьшуеться за наявностi концентратора напружень та при застосуваннi катодное поляризацИ. Встановлено деяк вiдмiнностi у сприйнятливостi до КРН при потенцiалi - 1,0 В вдносно хлорсрiбного електроду порiвняння) трубног сталi X70 ргзно1 технологи ви-робництва. При однаковш комбтацп чинниюв найбшьший вплив на чутливiсть до КРН обумовлюе наяв-тсть концентратора напружень
Ключовi слова: трубна сталь, поляризацiя, деформащя з повшьною швидюстю, катодний захист, коро-зтне розтрккування вiд напруження
Copyright © 2019, L. Nyrkova, A. Rybakov, S. Melnychuk, S. Osadchuk. This is an open access article under the CC BY license (http://creativec0mm0ns.0rg/licenses/by/4.0).
f N
ТЕХН1ЧН1 НАУКИ
v у
1. Introduction
Underground pipelines ensure an efficient and safe way of oil and gas transportation at long distances. Gas oil pipelines is a heterogeneous system, in which during contact with a corrosive and aggressive environment, the of local corrosion processes is thermodynamically probable. In the presence of mechanical stresses, the number types of probable fractures are expanding. One of the most dangerous and difficult-to-predict types of fractures in the main pipelines, which directly deteriorates the reliability of operation of the gas transport system (GTS), is stress-corrosion cracking (SCC) [1, 2]. Therefore, the study of this phenomenon, which is resulting in accidents, has an important scientific and practical significance.
2. Literature review
Depending on the properties of the medium, two types of SCC are distinguished: at high pH [3, 4] and near-neutral pH [5, 6]. Researchers proved that at high pH SCC proceeds in an intergranular mechanism [7], and at near-neutral pH its nature is transgranular [8].
SCC propagates at the simultaneous action of three groups of factors [9]: mechanical stress [10, 11], external environment [12] and properties of the metal [13]. The pipes, used in the section of a pipeline, even with the same chemical composition can have a slight difference in their corrosion-mechanical properties. Some of the researchers believe that the SCC development can be stopped by de-
signing and applying special grades of steel. Undoubtedly, this will increase the resistance of pipe steels to SCC, but will not completely solve the problem.
Despite the development and implementation of the methods, which allow to predict the propagation of corrosion, including the stress-corrosion cracking, thus contributing to a decrease in the overall level of accidents in the main pipelines, a share of fractures as a result of SCC propagation continues to be high. Therefore, it was considered expedient to conduct a study of sensitivity of pipe steel to SCC at a complex influence of different factors.
3. The aim and objectives of the study
The conducted researches aimed to determine the susceptibility to SCC of pipeline steel of a controllable rolling in the conditions of complex influence of factors, in the presence of some difference in the technology of pipe manufacturing.
To achieve the stated goal, the following tasks were set and fulfilled:
- to investigate the corrosion-mechanical properties of pipe steel X70 of a controllable rolling of different manufacturers under conditions of complex influence of factors, in particular: the corrosive environment, potential (Ecor, -1,0V, -2,0 V), the accumulated of cyclic stresses, the presence of stress concentrator;
- to evaluate the susceptibility to SCC of pipe steel X70 of controllable rolling of different manufactur-
ers under the influence of the combination of stress-corrosion factors in the range of potentials from the corrosion potential to the potential -2.0 V in a medium with near neutral pH.
4. Materials and methods of research
The object of investigations were the specimens of a pipe steel of X70 type of a controllable rolling, made
from the pipes being in operation (for about 40 years), having a diameter of 1420 mm and a wall thickness of 15.7 mm, conventionally named A and B.
The test solution was an NS4 solution + sodium-potassium phosphate buffer solution in the ratio of 9:1. Composition of NS4 is the following (g/l): 0.037 KCl + 0.559 NaHCO3 + 0.008 CaCl2 + 0.089 MgSO4, pH 8.0 [14].
Fig. 1. Sketch of the specimen for testing at a slow strain rate deformation
According to GOST 9.901-1, the method of slow strain rate deformation was applied. Plane specimens, Fig. 1, were subjected to tension in air and in the solution at a rate of 10-6 s-1 in the rupture testing machine AIMA -5-1. The cross-sectional area of a test part of the specimens in the initial state was 9 mm2. The tests were carried out at a corrosion potential, at the potentials -1.0 VAg/Aga and -2.0 VAg/Aga (relative to chlorine-silver electrode of comparison). A part of the specimens was subjected to cycling in an elastic region in the range of boundary stresses from 0.4 to 0.8<ys (<ys is yield strength) at a frequency of 10 Hz during 105 cycles, the other part of specimens was tested without preliminary cycling (further - specimens in the initial state). To accelerate the initiation of a stress-corrosion crack on the specimen, a local corrosion defect (further LCD) V-shape form with a depth from 0.25 mm to 0.3 mm, mechanically applied on one of the surfaces of the specimen was simulated.
The potential was controlled by potentiostat PI-50-1.1 and the programmer PR-8. The stresses, elongation of the specimen e and test duration were controlled during corrosion-mechanical tests.
5. Experimental results and discussion
5.1. Chemical composition and structure of the pipes
The chemical composition of the metal of the pipes under investigated is shown in Table 1. It is seen that the base metal of the pipe A is a low-carbon steel, microalloyed with vanadium and niobium, which accord-
ing to its chemical composition meets the requirements of TS 14-3-995-81 [15] to the X70 steel category.
The mechanical characteristics of the base metal of pipes under investigation were nearly the same and given below:
- yield strength, ays: 498-513 MPa (according to TS 14-3-995-81, not lower than 441 MPa);
- ultimate rupture strength, ar: 600-603 MPa (according to TS 14-3-995-81, not lower than 588 MPa);
- relative elongation, e: 21.5-24.2 % (the standard value is not lower than 20 %);
- impact toughness (KCV-15): 224-227 J/cm2 (standard value is not lower than 78.4 J/sm2).
In general, the base metal of the pipe under investigated at the standard values of strength, ductility and impact strength (<ys, ar, <ys/ar 85, KCV-15, KCU-60) meets the requirements of TS 14-3-995, according to which this pipe was manufactured, and the requirements of SNiP 2.05.06 [16].
The microstructure of the metal in both pipes (Fig. 1) is ferrite-pearlite with a slight structural heterogeneity at different areas of the sheet across its thickness (near the outer surface, as compared to other areas, ferrite grain is somewhat smaller and more elongated along the rolling), which is inherent for the steel of a controllable rolling.
The elongation of ferrite grains in the direction of rolling is very small.
Table 1
Chemical composition of the base metal of the investigated samples of pipes
Samples' characteristics Mass fraction of elements, %
C Mn Si S P Al Ni Mo Ti V Nb Cr
Pipe А 0.0890.101 1.331.45 0.2380.272 0.0040.005 0.0120.017 0.0310.032 0.04 0.03 0.004 0.050.06 0.027 0.04
Pipe B 0.119 1.48 0.357 0.003 0.016 0.034 0.05 0.03 0.005 <0.02 0.028 0.05
TS 14-3-99581 Not more than
0.12 1.70 0.50 0.010 0.020 0.050 - 0.30 - 0.08 0.06 -
a
Fig. 1. Microstructure of the base metal
Ferrite grain corresponds to 9-10 number for the pipe A and 10-11 number for the pipe B (except for individual grains of 9 number) according to GOST 5639 [17]. According to GOST 5640 [18], banded orientation of the base metal in the pipes A and B was evaluated by the ball 4, row A and by the ball 2, row B, respectively. The amount and dimensions of a perlitic structural component in the metal of the pipe B are slightly smaller than in the metal of the pipe A.
b
of the pipes: a - pipe A; b - pipe B.
The contamination of non-metallic inclusions in the base metal of both pipes is insignificant, which is typical for the pipe steel of the investigated type. The non-metallic inclusions mainly are line oxides and non-deformable silicates. Almost all of the inclusions are globulized; coarse elongated inclusions are absent. As it is seen from Table 2, the contamination of the non-metallic inclusions in the base metal of pipe A is somewhat higher than in the pipe B.
Table 2
Non-metallic inclusions in the base metal of the pipes samples under investigation
Sample characteristics Ball according to GOST 1778 [19]
oxides silicates sulfides
spot line plastic non-deformable
Pipe A 1 (scale а) 2 (scale b) 1 (scale b) 2 (scale b) 1 (scale а)
Pipe B 1 (scale а) 1 (scale b) 0 (scale b) 1 (scale b) 0.5 (scale а)
Therefore, the microstructure of the pipes under investigation is similar, namely ferrite-perlitic, with the exception of slight differences: for the pipe A, a higher contamination of the non-metallic inclusions in base metal, larger ferrite grains and somewhat larger banded orientation are peculiar.
5.2. Slow strain rate tests and the methodical approach to the estimation of SCC susceptibility
During the corrosion-mechanical tests, different combinations of stress-corrosion factors (corrosion-aggressive medium, potential, accumulated cyclic stresses, presence of stress concentrator) were simulated and the sensitivity of the pipe steel to SCC was evaluated under the mentioned conditions.
After rapture of the samples, their cross-sectional area was determined. The degree of sensitivity to SCC was evaluated according to the dimensionless coefficient Ks, which is equal to the ratio of relative reduction coefficient of the sample in air to relative reduction coefficient of the sample in the solution by the formula:
W
Ks = — s —
p
- =
Sö S1 Sn
(1)
(2)
where ¥n and ¥ is the relative reduction coefficient of the samples, respectively, in air and in the solution, S0 is the cross-section area of the samples before tests, mm2; S is the cross-section area of the samples in the place of fracture after tests in air Sjn or in the solution SjP, mm2.
To simulate the effect of cyclic stresses during the long-term operation of the gas pipeline, the samples were preliminary cycled in the range of boundary stresses from 0.4 to 0.8at at a frequency of 10 Hz during 105 cycles.
It is commonly known that a stress-corrosion crack initiates from local stress concentrators, for example, in the form of local corrosion damage (further - LCD). Therefore, to accelerate its initiation in the laboratory conditions, on the samples, V-shaped LCD of ~0.2 mm depth was simulated, which was applied to one of the surfaces of the sample by mechanical method. It was assumed that the state of the sample with accumulated stresses and with the simulated LCD could be compared with the state of the MG under operation.
5.2.1. Investigation and estimation of the susceptibility of pipeline steel to SCC at corrosion potential
The curves of mechanical fracture in air and corrosion-mechanical fracture in the solution at the corrosion potential of the samples made from the pipe A are shown in Fig. 2, a and from the pipe B - in Fig. 2, b.
The fracture of the samples in air was ductile, Fig. 3 a, 3 b (photo 1), as is evidenced by the typical neck-down near the place of fracture. For the samples made from the pipe A and B, respectively, the fracture time was ~19.5 h and ~20 h, the cross-section area was ~3.97 mm2 and ~2.91 mm2, the relative reduction coefficient was 56 % and 68 %. After the tests in the solution at the corrosion potential, a decrease in the fracture time was observed: for the samples from the pipe A - to ~18.3 h and for the samples from the pipe B, the fracture time remained the same. The relative reduction coefficient was decreased to 45 % and 56 %, respectively. Under these conditions, the coefficient of sensitivity to SCC KS in the metal of both pipes was almost the same - 1.24 and 1.21. Like in air, the character of fracture was ductile (Fig. 3, a, b, photo 2).
Р, N 4600
4400
4200
4000
3800
3600
3400
0,000 0,001 0,002 0,003 0,004 0,005 0,006
s, m
Р, N.
4600 4400 4200 4000 3800 3600 3400
0,000 0,001 0,002 0,003 0,004 0,005 0,006
s, m
b
Fig. 2. Mechanical fracture curves in air and corrosion-mechanical fracture curves of the X70 pipe steel samples made from the pipe A and the pipe B in the NS4 solution under the influence of a complex of stress-corrosion factors at the corrosion potential: a - pipe A; b - pipe B; 1 - sample in air, 2 - sample in the initial state, 3 - sample after cycling, 4 - sample in the initial state with LCD, 5 - sample after cycling with LCD
a
b
Fig. 3. Photos of fractures of the X70 pipe steel samples made from the pipe A and the pipe B after mechanical tests in air and corrosion-mechanical tests in the solution at the influence of a complex of stress-corrosion factors on the potential of corrosion:
a - pipe A; b - pipe B; 1 - sample in air, 2 - sample in the initial state, 3 - sample after cycling, 4 - sample in the initial state with LCD, 5 - sample after cycling with LCD
A preliminary cycling of samples in the elastic region very little changed the corrosion-mechanical properties of the steel compared to the initial state: the fracture time was equal to ~17.0 h and ~19.5 h, the cross-section area was equal ~4.02 mm2 and ~3.77 mm2, and the coefficient Ks =1.02 for the pipe A and Ks =1.17 for the pipe B. The fracture character of the samples remained ductile (Fig. 3, a and 3, b, photo 3).
At the presence of stress concentrator, the regularities of the fracture changed significantly: the time of fracture decreased by almost twice: to ~9.5 h for the pipe A and to ~12 h for the pipe B, the cross-section area increased to 5.90 mm2 and 4.83 mm2. Among the noted changes in the character of fracture (Fig. 3a and 3b, photo 4), there are a lower plastic deformation of the samples, which correlated with an increase in the degree of sensitivity to SCC: the coefficient Ks was equal 1.65 for the pipe A and 1.48 for the pipe B. The regularities of fracture of the samples after preliminary cycling and in the presence of LCD were as follows: the time of fracture remained almost unchanged as compared to the samples
without preliminary cycling and was, ~10.0 h for the pipe A and ~9.5 h for the pipe B, but the cross-section area somewhat decreased to 4.69 mm2 and 3.90 mm2, the degree of sensitivity to SCC was: for the pipe A the coefficient Ks=1.22 and for the pipe B - Ks=1.19. The character of fracture was similar to the character of fracture of the same samples without preliminary cycling (Fig. 3 a, b, photo 5).
At the corrosion potential, the corrosion-mechanical properties of steel made from pipe A and B having slight structural differences, including those after cycling and in the presence of LCD, were almost similar: the fracture was ductile, the sensitivity to SCC was low, the coefficient Ks varied from 1.21 to 1.65 for the samples from the pipe A and from 1.17 to 1.48 for the samples from the pipe B (Fig. 8, a).
The sensitivity to SCC at the corrosion potential was most strongly influenced by LCD: in the presence of stress concentrator the decreasing of the fracture time and a part of plastic deformation in the fracture is noted.
5.2.2 Investigation and estimation of the susceptibility of pipeline steel to SCC at the potential -1.0
VAg/AgCl
The fracture curves are presented in Fig. 4, a, b.
At the potential -1.0 VAg/AgCi, the fracture time did not change much compared to fracture time of the samples at the corrosion potential: for the samples made from the pipe A it was equal to ~18.0 h, for the samples from the pipe B near ~19.0 h. However, an increasing of the cross-section for the samples made from the pipe A to ~6.07 mm2 was noted; whereas the cross-section of the
samples from the pipe B almost did not change and was equal to ~3.92 mm2. Under these conditions an increasing of the coefficient Ks for the metal made from the pipe A to near 1.7 was observed. For the metal of the pipe B, the value of the coefficient remained almost the same as it was at the corrosion potential, Ks =1.21.
Significant changes in the fracture character were noted: for the sample made from the pipe A, a lower reduction was peculiar, which correlated with the coefficient of sensitivity to SCC (Fig. 5, a, b, photo 2).
s, m
a
0,000 0,001 0,002 0,003 0,004 0,005 0,006
s, m
b
Fig. 4. Mechanical fracture curves in air and corrosion-mechanical fracture curves of the X70 pipe steel samples made from the pipe A and the pipe B, in the NS4 solution under the influence of a complex of stress-corrosion factors at the potential -1.0 VAg/AgCl: a - pipe A; b - pipe B; 1 - sample in air, 2 - sample in the initial state, 3 - sample after cycling, 4 - sample in the initial state with LCD, 5 - sample after cycling with LCD
b
Fig. 5. Photos of fractures of the X70 pipe steel samples made from the pipe A and the pipe B after mechanical tests in air and corrosion-mechanical tests in the solution at the influence of a complex of stress-corrosion factors at the potential - 1.0 VAg/AgCl:
a - pipe A; b - pipe B; 1 - sample in air, 2 - sample in the initial state, 3 - sample after cycling, 4 - sample in the initial state with LCD, 5 - sample after cycling with LCD
A preliminary cycling of the samples in the elastic region had little effect on the corrosion-mechanical properties of the samples made from the pipes A and B as compared to the initial state: the fracture time was near ~17.0 h and ~20.0 h, the cross-section area was equal to 5.94 mm2 and 4.35 mm2, the coefficient was Ks =1.65 for the pipe A and Ks =1.31 for the pipe B. The fracture character remained ductile for the samples from the pipe B (Fig. 5, b, photo 3). For the samples from the pipe A a less plastic deformation is peculiar (Fig. 5, a, photo 3).
Similarly as at the corrosion potential, in the presence of stress concentrator, the regularities of fracture differed significantly: the fracture time significantly decreased to ~6.5 h (pipe A) and to 5.5 h (pipe B), the cross-section area increased to 6.34 mm2 and 5.71 mm2 and the degree of sensitivity to SCC was: Ks=1.87 for the pipe A and Ks =2.13 for the pipe B.
The fracture also took place in a different way: for the samples, a lower reduction coefficient was noted, which corresponded to the increasing in the values of the coefficient of sensitivity to SCC (Fig. 5, a, b, photo 4).
For the samples after the preliminary cycling and in the presence of LCD, the corrosion-mechanical properties were similar to those, which were on the samples without cycling and other compared to the properties of the samples in the initial state: the fracture time was ~2.5 h and ~4.5 h, the cross-section area was increase up to
~6.5 mm2 and ~6.37 mm2, the degree of sensitivity to SCC was: for the pipe A, Ks =2.0 and for the pipe B, Ks =2.34. The fracture character was similar to the fracture character of the same samples without preliminary cycling (Fig. 5a and 5b, photo 5).
Thus, it was shown that at the potential - 1.0 VAg/AgCl, which approaches the maximum protection one in accordance to DSTU 4219 [20], some differences in the sensitivity of the pipe steel to SCC, including that being under a long operation, may occur. It was assumed that higher ductile properties of the steel at the cathode potential may be associated with a lower contamination by non-metallic inclusions. But at the influence of a number of other factors, the ductility of this steel may be deteriorated, which was observed in the presence of LCD.
5.2.3 Investigation and estimation of the susceptibility of pipeline steel to SCC at the potential -2.0
VAg/AgCl
The experience showed that during operation, the increasing of the potential to higher (at the absolute value) than the maximum protection value is possible, the so-called "overprotection" phenomenon. Therefore, it was considered expedient to study the sensitivity of the pipe steel to SCC under the mentioned conditions. The curves of fracture are presented in Fig. 6, a, b.
a
At the potential -2.0 VAg/AgCl, the corrosion-mechanical properties (Fig. 6a, 6b) and the character of fracture (Fig. 7, a, b) changed, which was probably predetermined by the change in the mechanism of SCC.
First, the fracture time decreased compared to the fracture time at the corrosion potential and at -1.0 VAg/AgCl to ~14.0 h for the samples from both pipes and, accordingly, the cross-section for the samples made from
the pipe A was increased to ~7.55 mm2, and for the samples made from the pipe B to ~6.67 mm2. This naturally resulted in the increasing of sensitivity to SCC, as was evidenced by the value of Ks: for the samples made from the pipe A, Ks=3.5 and from the pipe B, Ks =2.61. The fracture of the samples of the pipes A and B occurred either almost without plastic deformation, or with a very slight reduction coefficient (Fig. 7, a, b, photo 2).
s, m
a
s, m
b
Fig. 6. Mechanical fracture curves in air and corrosion-mechanical fracture curves of the X70 pipe steel samples made from the pipe A and the pipe B, in the NS4 solution under the influence of a complex of stress-corrosion factors at the potential - 2.0 VAg/AgCl: a - pipe A; b - pipe B; 1 - sample in air, 2 - sample in the initial state, 3 - sample after cycling, 4 - sample in the initial state with LCD, 5 - sample after cycling with LCD.
2
b
Fig. 7. Photos of fractures of the X70 pipe steel samples made from the pipe A and the pipe B after mechanical tests in air and corrosion-mechanical tests in the solution at the influence of a complex of stress-corrosive factors at the potential - 2.0 VAg/AgCl: a - pipe A; b - pipe B; 1 - sample in air, 2 - sample in the initial state, 3 - sample after cycling, 4 - sample in the initial state with LCD, 5 - sample after cycling with LCD
The preliminary cycling had a little effect on the corrosion-mechanical properties of the samples made of the pipes A and B as compared to the initial state: the fracture time was ~11.0 h and ~ 11.6 h, the cross-section
area was ~6.9 mm and ~7.62 mm .
Ks =2.43
for the
pipe A and Ks =4.5 for the pipe B. As in the samples
without a preliminary cycling, during fracture, a plastic deformation was almost not observed (Fig. 8a and 8b, photo 3).
Thus, the shifting of the cathodic protection potential from -1.0 VAg/AgCl to - 2.0 VAg/AgCl leads to changing of the fracture character of (the part of brittle component increases), which causes an increasing of the sensitivity of the pipe steel to SCC, including the samples after cycling (Fig. 8c).
ks
1,6
К
K
X, h
20
-15
-10
Air Ecor Ecor Ecor Ecor, cycling cyclmg defect defect
x, h
20
15 10
air -1,0 V Cycling LCD Cycling
-1,0 V -1,0 V LCD, -1,0 V
b
15
10
Air
-2,0 V
-2,0 V cycling
Fig. 8. Degree of susceptibility to SCC (columns) and fracture time (lines) of the X70 pipe steel samples of different manufacturers at the influence of a complex of stress-corrosion factors: a - at the corrosion potential; b - at the potential -1.0 VAg/AgCl; c - at the potential -2.0 VAg/AgCl
a
a
5
h
c
6. Conclusions
1. The sensitivity of the pipe steel of X70 type of a controllable rolling to SCC was investigated in the conditions of a complex influence of factors: corrosive medium, potential (EOT, -1.0 VAg/AgCl, -2.0 VAg/AgCl), accumulated cyclic stresses and the presence of stress concentrator.
2. It was established that this steel under cathodic polarization is susceptible to SCC, which grows at the increasing of the potential (at the absolute value). It was shown that under a protective potential, approaching the maximum value according to DSTU 4291, some differences in the corrosion-mechanical properties of the mentioned steel may be revealed, namely: elevated or lowered sensitivity to SCC.
3. It was assumed that such features are predetermined by the contamination by non-metallic inclusions, banded orientation of the structure and grain size. At a
higher protection potential, this difference is flattened. At the same combination of other factors, the greatest influence on sensitivity to SCC is predetermined by the presence of stress concentrator.
Acknowledgements
The work was carried out within the framework of the departmental order program of the National Academy of Sciences of Ukraine by the E.O. Paton Electric Welding Institute in 2010-2012 (fundamental research works) "Improvement of operational reliability of pipes and systems in the main pipelines on the basis of development of new multi-arc welding processes, investigation of processes of initiation and propagation of stress-corrosion defects and development of the basic provisions of the rules on designing and operation of double-wall tanks" (State registration number 0110U001621).
References
1. Antonov, V. G., Arabei, A. B., Voronin, V. N., Dolgov, I. A., Kantor, M. M., Knoshinski, Z., Surkov, IU. P.; Arabei, A. B., Knoshinski, Z. (Eds.) (2006). Korrozionnoe rastreskivanie pod napriazheniem trub magistralnykh gazoprovodov: atlas. Moscow: Nauka, 105.
2. Frank Cheng, Y. (2013). Stress Corrosion Cracking of Pipelines. Hoboken: John Willey&Sons Publishing, 257.
3. Song, F. M. (2009). Predicting the mechanisms and crack growth rates of pipelines undergoing stress corrosion cracking at high pH. Corrosion Science, 51 (11), 2657-2674. doi: http://doi.org/10.10167j.corsci.2009.06.051
4. Wang, J., Atrens, A. (2003). SCC initiation for X65 pipeline steel in the "high" pH carbonate/bicarbonate solution. Corrosion Science, 45 (10), 2199-2217. doi: http://doi.org/10.1016/s0010-938x(03)00044-1
5. Chu, R., Chen, W., Wang, S.-H., King, F., Jack, T. R., Fessler, R. R. (2004). Microstructure Dependence of Stress Corrosion Cracking Initiation in X-65 Pipeline Steel Exposed to a Near-Neutral pH Soil Environment. Corrosion, 60 (3), 275-283. doi: http://doi.org/10.5006/L3287732
6. Zhang, C., Cheng, Y. F. (2009). Synergistic Effects of Hydrogen and Stress on Corrosion of X100 Pipeline Steel in a Near-Neutral pH Solution. Journal of Materials Engineering and Performance, 19 (9), 1284-1289. doi: http://doi.org/10.1007/s11665-009-9579-3
7. Arafin, M. A., Szpunar, J. A. (2009). A new understanding of intergranular stress corrosion cracking resistance of pipeline steel through grain boundary character and crystallographic texture studies. Corrosion Science, 51 (1), 119-128. doi: http://doi.org/10.1016/jxorsci.2008.10.006
8. Parkins, R. N., Blanchard, W. K., Delanty, B. S. (1994). Transgranular Stress Corrosion Cracking of High-Pressure Pipelines in Contact with Solutions of Near Neutral pH. Corrosion, 50 (5), 394-408. doi: http://doi.org/10.5006/L3294348
9. Egbewande, A., Chen, W., Eadie, R., Kania, R., Van Boven, G., Worthingham, R., Been, J. (2014). Transgranular crack growth in the pipeline steels exposed to near-neutral pH soil aqueous solutions: Discontinuous crack growth mechanism. Corrosion Science, 83, 343-354. doi: http://doi.org/10.1016/jxorsci.2014.02.032
10. Chen, W., Vanboven, G., Rogge, R. (2007). The role of residual stress in neutral pH stress corrosion cracking of pipeline steels - Part II: Crack dormancy. Acta Materialia, 55 (1), 43-53. doi: http://doi.org/10.1016/j.actamat.2006.07.021
11. Tang, X., Cheng, Y. F. (2009). Micro-electrochemical characterization of the effect of applied stress on local anodic dissolution behavior of pipeline steel under near-neutral pH condition. Electrochimica Acta, 54 (5), 1499-1505. doi: http://doi.org/10.1016/j.electacta.2008.09.037
12. Harris, N., Askarov, G. (2006). Activation of corrosion processes on main gas pipelines of large diameter with impulse temperature change. Oil and gas business.
13. Asahi, H., Kushida, T., Kimura, M., Fukai, H., Okano, S. (1999). Role of Microstructures on Stress Corrosion Cracking of Pipeline Steels in Carbonate-Bicarbonate Solution. Corrosion, 55 (7), 644-652. doi: http://doi.org/10.5006/L3284018
14. Szklarska-Smialowska, Z., Xia, Z., Rebak, R. B. (1994). Technical Note:Stress Corrosion Cracking of X-52 Carbon Steel in Dilute Aqueous Solutions. Corrosion, 50 (5), 334-338. doi: http://doi.org/10.5006/L3294341
15. TU 14-3-995-81 Truby stalnye elektrosvarnye priamoshovnye ekspandinovannye diametrom 1420 mm iz stali marki X-70. Tekhnicheskie usloviia.
16. SNiP 2.05.06-85 Magistralnye truboprovody. Available at: http://profidom.com.ua/v-2/v-2-3/1653-snip-2-05-06-85-magistralnyj e-truboprovody
17. GOST 5639-82 Steels and alloys. Methods for detection and determination of grain size. Available at: http://docs.cntd.ru/ document/1200005473
18. GOST 5640-68 Steel. Metallographic method for determination of microstructure of sheets and bands. Available at: http://docs.cntd.ru/document/1200004803
19. GOST 1778-70 Steel. Metallographic methods for the determination of nonmetallic inclusions. Available at: http://gostrf.com/normadata/1/4294835/4294835064.pdf
20. DSTU 4219-2003. Steel pipe mains general requirements for corrosion protection. Available at: https://dnaop.com/html/34129/doc-%D0%94%D0%A1%D0%A2%D0%A3_4219-2003
Received date 28.08.2019 Accepted date 11.09.2019 Published date 31.10.2019
Lyudmila Nyrkova, PhD, Head of Department, Department of Welding of Oil and Gas Pipes, E.O. Paton Electric Welding Institute of the National Academy of Sciences of Ukraine, Hiioma de Boplana str., 11, Kyiv, Ukraine, 2230
E-mail: lnyrkova@gmail.com
Anatoliy Rybakov, PhD, Senior Research Fellow, Department of Welding of Oil and Gas Pipes,E.O. Paton Electric Welding Institute of the National Academy of Sciences of Ukraine, Hiioma de Boplana str., 11, Kyiv, Ukraine, 2230
E-mail: rybakov@paton.kiev.ua
Sergey Mel'nychuk, Engineer, Department of Welding of Oil and Gas Pipes, E.O. Paton Electric Welding Institute of the National Academy of Sciences of Ukraine, Hiioma de Boplana str., 11, Kyiv, Ukraine, 2230 E-mail: sergeymelnichuk33@gmail.com
Svitlana Osadchuk, Junior Researcher, Department of Welding of Oil and Gas Pipes, E.O. Paton Electric Welding Institute of the National Academy of Sciences of Ukraine, Hiioma de Boplana str., 11, Kyiv, Ukraine, 2230 E-mail: svetlanaosadchuk@meta.ua
УДК 550.423
DOI: 10.15587/2313-8416.2019.179590
ВМ1СТ ВАЖКИХ МЕТАЛ1В У НАФТАХ ПРИКАРПАТСЬКО1 ТА ДН1ПРОВСЬКО-ДОНЕЦЬКО1 НАФТОГАЗОНОСНИХ ПРОВ1НЦ1Й УКРА1НИ
А. М. брофеев
Наведено методику та результати до^дження eMicmy важких Memanie у зразках нафти з двох основ-них нафтогазоносних провтцш Укра'ти. Проведене оглядове моделювання ймовiрних шляхiв надходжен-ня важких мemaлiв у вуглеводневу сировину. За результатами до^дження, зроблене nорiвняння власти-востей в зaлeжносmi вiд хiмiчного вмiсmу зразюв. Визначет ймовiрнi причини розбiжносmeй концент-рацш важких мemaлiв у нафтах з ргзних гeологiчних структур
Ключовi слова: важю метали, рентгенофлуоресцентна спeкmроскопiя, гeохiмiя нафти, хiмiчний склад, мemaлооргaнiчнi сполуки
Copyright © 2019, A. Jerofieiev.
This is an open access article under the CC BY license (http://creativecommons.org/licenses/by/4.0).
1. Вступ
Нафта та природн гази е важливими джерела-ми енергетично! та вуглеводнево! сировини, що ви-користовуються не лише для паливно-енергетичних потреб суспшьства, а також для оргашчного синтезу матерiалiв. О^м, власне, вуглеводшв, нафти вмь щують метал1чш хiмiчнi елементи, що найчаслше представляють собою И мшрокомпонентний склад. Вивчення джерел та умов накопичення металiв у на-фтах е важливим фактором визначення генезису вуг-леводшв, а також процеав забруднення навколиш-нього середовища. Це обумовлюе актуальшсть про-ведених дослвджень.
2. Лггературний огляд
Проблему вмюту важких металiв у нафтах почали вирiшувати з середини 20 столитя. Серед
останшх публшащй, присвячених цш тематищ, слад згадати як шоземш, так i вичизняш роботи.
Ще у 2007 рощ була опублшована про вмют ванадш та шкелю в природних нафтах свггу [1]. В нш були детально розглянуп результати дослвджень концентрацш важких металiв в нафтах, що стосува-лись фундаментальних дослвджень в галузi И похо-дження.
У 2008 рощ з'являеться робота, присвячена ресурснш базi супутшх компонентiв важких нафт [2]. В нш автор роздивився сучасний стан ощнки запасiв супутнiх компонентiв нафти, як джерел високояшс-но! рiдкометалiчноi сировини.
У 2010 роцi опублжоваш результати досль дження глибинно! зональносп в збагаченностi вугле-воднiв важкими елементами-домiшками. [3] В сво!х дослвдженнях автор вказуе на вiдмiнностi вмюту ва-