Flow-Induced Carbon Dioxide and Hydrogen Sulfide Corrosion Studies Using the Dynamic Field Tester in Crude Oil Wells

CORROSION ◽  
2002 ◽  
Vol 58 (10) ◽  
pp. 881-890 ◽  
Author(s):  
S. E. Hernández ◽  
S. Hernández ◽  
H. Rincón ◽  
J. R. Vera
Keyword(s):  
Carbon Dioxide ◽  
Hydrogen Sulfide ◽  
Crude Oil ◽  
Oil Wells ◽  
Dynamic Field ◽  
Corrosion Studies ◽  
Sulfide Corrosion ◽  
Hydrogen Sulfide Corrosion

New, effective carbon dioxide and hydrogen sulfide corrosion inhibitors based on white phosphorus, sulfur, alcohols, and amines

2013 ◽  
Vol 53 (2) ◽  
pp. 139-143 ◽  
Author(s):  
E. S. Batyeva ◽  
O. V. Ugryumov ◽  
O. A. Varnavskaya ◽  
Yu. P. Khodyrev ◽  
E. V. Platova ◽  
...  
Keyword(s):  
Carbon Dioxide ◽  
Hydrogen Sulfide ◽  
Corrosion Inhibitors ◽  
White Phosphorus ◽  
Sulfide Corrosion ◽  
Hydrogen Sulfide Corrosion

scholarly journals Research on hydrogen-induced cracking behavior of normalized pipeline steel

2018 ◽  
Vol 175 ◽  
pp. 01027
Author(s):  
Hai Zhang ◽  
Shaopo Li ◽  
Wenhua Ding ◽  
Ning Hao
Keyword(s):  
Hydrogen Sulfide ◽  
Corrosion Test ◽  
Pipeline Steel ◽  
Plate Thickness ◽  
Hardness Test ◽  
Propagation Path ◽  
Cracking Behavior ◽  
Hydrogen Induced Cracking ◽  
Sulfide Corrosion ◽  
Hydrogen Sulfide Corrosion

Hydrogen sulfide corrosion test was used to test the hydrogen-induced cracking sensitivity of the normalized BNS pipeline steel. The microstructure and morphology of hydrogen induced crack(HIC) of the normalized BNS pipeline steel after hydrogen sulfide corrosion test were observed with optical microscopy(OM), scanning electron microscopy(SEM). Combined with electron probe microanalyzer(EPMA) and hardness test, the hydrogen-induced cracking behavior of BNS pipeline steel was studied from the aspects of microstructure, crack morphology, center segregation and harness. The results showed that the pearlite band with high hardness caused by center segregation of C and Mn was the main crack initiation and propagation path for the long-size and linear shape hydrogen induced crack at the center of plate thickness, and the type of crack propagation was transgranular. Some tiny hydrogen induced crack nucleated from the small calcium-aluminate inclusion and the tiny hydrogen induced crack would not propagate to form long-size cracks with no suitable propagation path existing around the inclusion.

High Temperature Hydrogen Sulfide Corrosion★

CORROSION ◽  
1956 ◽  
Vol 12 (1) ◽  
pp. 22-32 ◽  
Author(s):  
E. B. BACKENSTO ◽  
R. D. DREW ◽  
C. C. STAPLEFORD
Keyword(s):  
Hydrogen Sulfide ◽  
High Temperature ◽  
Carbon Steel ◽  
Carbon Steels ◽  
Effect Of Temperature ◽  
Sulfide Concentration ◽  
Wide Range ◽  
Sulfide Corrosion ◽  
Hydrogen Sulfide Corrosion ◽  
Hydrogen Sulfide Concentration

Abstract High temperature hydrogen sulfide corrosion of carbon steel and low chrome alloys has become a serious problem in the petroleum industry in connection with the increasing use of high pressure hydrogenation and dehydrogenation processes for upgrading petroleum fractions. The effect of temperature, pressure and hydrogen sulfide concentration on the corrosion rate of a wide range of commonly used carbon steels and alloys has been determined in laboratory tests. It has been established that the low chrome alloys (up to 5 percent chromium) which have been used to combat sulfur corrosion in fractionation and cracking equipment, show little or no advanage over carbon steel in resisting attack by hydrogen sulfide. Of the conventional alloy steels tested, only the 18-8 chrome nickel and higher alloys have shown good resistance to this type of corrosion over a wide range of pressure, temperature and hydrogen sulfide concentration. It was found that aluminum coated steels also showed very good corrosion resistance. Three methods were proposed for minimizing hydrogen sulfide corrosion: (1) Reduction of hydrogen sulfide in process streams, (2) Use of chrome-nickel alloys, and (3) Protection of metals by aluminum coating.

Hydrogen sulfide corrosion inhibitor for hydrocracking units

1985 ◽  
Vol 21 (9) ◽  
pp. 439-441
Author(s):  
D. F. Varfolomeev ◽  
G. P. Naletova ◽  
N. M. Nikolaeva ◽  
N. K. Neprina ◽  
A. Z. Safin ◽  
...  
Keyword(s):  
Hydrogen Sulfide ◽  
Corrosion Inhibitor ◽  
Sulfide Corrosion ◽  
Hydrogen Sulfide Corrosion

Pyrophoric tendency of hydrogen sulfide corrosion product in oil tanks under aerobic condition

2013 ◽  
Vol 41 (1) ◽  
pp. 11-17 ◽  
Author(s):  
Bo Liu ◽  
Fenghua Zhang ◽  
Ping Li ◽  
Liyan Shang ◽  
Zhenhua Zhang ◽  
...  
Keyword(s):  
Hydrogen Sulfide ◽  
Corrosion Product ◽  
Aerobic Condition ◽  
Sulfide Corrosion ◽  
Oil Tanks ◽  
Hydrogen Sulfide Corrosion

Inhibition of hydrogen sulfide corrosion of steel in gas phase by tributylamine

2012 ◽  
Vol 64 ◽  
pp. 126-136 ◽  
Author(s):  
R.V. Kashkovskiy ◽  
Yu.I. Kuznetsov ◽  
L.P. Kazansky
Keyword(s):  
Hydrogen Sulfide ◽  
Gas Phase ◽  
Sulfide Corrosion ◽  
Corrosion Of Steel ◽  
Hydrogen Sulfide Corrosion

Synthesis of hydrogen sulfide corrosion inhibitors for oil production

2013 ◽  
Vol 53 (6) ◽  
pp. 423-425 ◽  
Author(s):  
A. M. Magerramov ◽  
M. R. Bairamov ◽  
Sh. B. Khoseinzade ◽  
M. A. Agaeva ◽  
G. M. Mekhtieva ◽  
...  
Keyword(s):  
Hydrogen Sulfide ◽  
Corrosion Inhibitors ◽  
Oil Production ◽  
Sulfide Corrosion ◽  
Hydrogen Sulfide Corrosion
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