Corrosion simulation via coupling computational fluid dynamics and NORSOK CO2 corrosion rate prediction model for an outlet header piping of an air-cooled heat exchanger

被引:20
作者
Dana, Mohammad Mahdi [1 ]
Javidi, Mehdi [1 ]
机构
[1] Shiraz Univ, Sch Engn, Dept Mat Sci & Engn, Shiraz 7134851154, Iran
关键词
CO2; corrosion; Computational fluid dynamics; NORSOK M-506; Simulation; Wet gas; CARBON-DIOXIDE CORROSION; FAILURE ANALYSIS; CHLORIDE CONTENT; GAS-PRODUCTION; FLOW; OIL; STEEL; WATER; PIPELINE;
D O I
10.1016/j.engfailanal.2021.105285
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
In this study CO2 corrosion of outlet header pipe of an air-cooled heat exchanger in a natural gas dehydration unit of a gas refinery was investigated by simulation via coupling computational fluid dynamics and NORSOK M-506 CO2 corrosion prediction model. The Euler-Euler approach incorporated with k-E model for the fluid turbulence was employed to simulate gas-liquid twophase flow. The simulation results were utilized as the inputs of NORSOK CO2 corrosion prediction model to calculate CO2 corrosion rate. Fluid streamlines, velocity, viscosity, density and temperature profiles and also the distribution of gas and liquid phases through the investigated outlet header pipe were calculated and a three-dimensional corrosion rate map was presented. The results showed that there is a good agreement between the data obtained by corrosion simulation and field observation. It was found here that coupling computational fluid dynamics and CO2 corrosion prediction models can successfully predict regional corrosion rates and determine locations susceptible to CO2 corrosion.
引用
收藏
页数:17
相关论文
共 52 条
[1]   Transient modeling of non-isothermal, dispersed two-phase flow in natural gas pipelines [J].
Abbaspour, Mohammad ;
Chapman, Kirby S. ;
Glasgow, Larry A. .
APPLIED MATHEMATICAL MODELLING, 2010, 34 (02) :495-507
[2]   Failure analysis of carbon dioxide corrosion through wet natural gas gathering pipelines [J].
Abd, Ammar Ali ;
Naji, Samah Zaki ;
Hashim, Atheer Saad .
ENGINEERING FAILURE ANALYSIS, 2019, 105 :638-646
[3]   The effect of acetic acid on the pit propagation in CO2 corrosion of carbon steel [J].
Amri, J. ;
Gulbrandsen, E. ;
Nogueira, R. P. .
ELECTROCHEMISTRY COMMUNICATIONS, 2008, 10 (02) :200-203
[4]   Evaluation of erosion-corrosion in multiphase flow via CFD and experimental analysis [J].
Bozzini, B ;
Ricotti, ME ;
Boniardi, M ;
Mele, C .
WEAR, 2003, 255 :237-245
[5]  
Burt V., 2015, Corrosion in the Petrochemical Industry
[6]  
Crolet J.-L., 1990, OFFSHORE TECHNOLOGY
[7]   Monitoring of trace chloride ions at different stages of the gas production process [J].
El Naggar, A. Y. ;
Moustafa, Y. M. ;
Faramawy, S. ;
Elfadly, A. M. ;
Abdullah, E. S. ;
Ebiad, M. A. .
ARABIAN JOURNAL OF CHEMISTRY, 2015, 8 (01) :15-24
[8]  
El-Naggar A.Y., 2014, INT J SCI, V3, P13
[9]  
El-Sherik AM, 2017, WOODHEAD PUBL SER EN, pXXXV
[10]   An electrochemical investigation on the effect of the chloride content on CO2 corrosion of API-X100 steel [J].
Eliyan, Faysal Fayez ;
Mohammadi, Farzad ;
Alfantazi, Akram .
CORROSION SCIENCE, 2012, 64 :37-43