In Situ Synthesis of 2-Phenylbenzimidazole as an Hydrogen Sulfide Corrosion Inhibitor of Carbon Steel

CORROSION ◽  
10.5006/0854 ◽  
2013 ◽  
Vol 69 (12) ◽  
pp. 1195-1204 ◽  
Author(s):  
Sh. Pournazari ◽  
M.H. Moayed ◽  
M. Rahimizadeh
Keyword(s):  
Hydrogen Sulfide ◽  
Carbon Steel ◽  
Corrosion Inhibitor ◽  
In Situ Synthesis ◽  
Sulfide Corrosion ◽  
Hydrogen Sulfide Corrosion

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

Optimization of synthesis of a sulfonate hydrogen sulfide corrosion inhibitor

2010 ◽  
Vol 46 (5) ◽  
pp. 363-366
Author(s):  
Z. R. Agaeva ◽  
K. I. Sadykhov ◽  
F. M. Velieva ◽  
I. G. Melikova
Keyword(s):  
Hydrogen Sulfide ◽  
Corrosion Inhibitor ◽  
Sulfide Corrosion ◽  
Hydrogen Sulfide Corrosion

Adsorption of Corrosion Inhibitor 1-Dodecylpyridinium Chloride on Carbon Steel Studied by in Situ AFM and Electrochemical Methods

2014 ◽  
Vol 53 (14) ◽  
pp. 5858-5865 ◽  
Author(s):  
Vedapriya Pandarinathan ◽  
Kateřina Lepková ◽  
Stuart I. Bailey ◽  
Thomas Becker ◽  
Rolf Gubner
Keyword(s):  
Carbon Steel ◽  
Corrosion Inhibitor ◽  
Electrochemical Methods ◽  
Dodecylpyridinium Chloride

Analysis of adsorption of carbon steel corrosion inhibitor in model stratum waters by polylogarithmic isotherm

2021 ◽  
pp. 20-26
Author(s):  
L.E. Tsygankova ◽  
◽  
N. Alshikha ◽  
M.V. Vigdorowitsch ◽  
I.V. Zarapina ◽  
...  
Keyword(s):  
Carbon Steel ◽  
Steel Corrosion ◽  
Oil Field ◽  
Energy Gradient ◽  
Double Layer Capacity ◽  
Sulfide Corrosion ◽  
As Adsorption ◽  
Hydrogen Sulfide Corrosion ◽  
Protective Effectiveness ◽  
Steel St3

Using the methods of gravimetry, potentiodynamic polarization, and impedance spectroscopy, the protective effectiveness of the inhibitory composition INCORGAZ-111 with respect to hydrogen sulfide corrosion of carbon steel St3 in NACE and Samotlor oil field model stratum waters has been studied. Surface coverage is determined on the basis of the electric double layer capacity in presence of the inhibitor. Its adsorption is interpreted using the polylogarithmic isotherm with a big energy gradient of adsorption centers, that indicates linear energy heterogeneity of the surface. The constants of adsorption equilibrium, the energy gradient and the energy dispersion of adsorption centers as well as adsorption free energy were calculated.

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.

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