Sarkhoon gas plant, located in south of Iran, has been installed to removal H2S contained in a high pressure natural gas stream. The solvent used for the H2S removal from gaseous stream is 34% by weight (wt%) Di-ethanol amine (DEA) solutions. Due to increasing concentration of heat stable salt (HSS) in solvent, corrosivity of amine solution had been increased. Reports indicated that there was corrosion on the shell of regeneration column. Because source formation of HSS was unknown, we decided to control the amount of HSS at the limit less than 3% wt amine solvent. Therefore, two small columns were filled by strong anionic base and carbon active, and then polluted amine was passed through beds. Finally a temporary amine recovery package on ...
This paper includes the significant on-site experience of the authors related to problems faced in a...
Monoethylene glycol (MEG), a common hydrate inhibitor in natural gas transportation pipelines is usu...
Abstract The gas sweetening unit of phase 2 and 3 in South Pars Gas Field (Asalouyeh, Iran) was firs...
International audienceIn the oil and gas industry, acid gas removal is required for the treatment of...
"""sour"" natural gases are ""sweetened"" by reaction with alkaline solutions to remove H2S, CO, and...
International audienceProcesses using amine solvents for the removal of CO 2 have long been used for...
Amines are used in refineries and gas plants around the world to remove both H2S and CO2 from feed g...
International audienceCorrosion represents one of the most important operational issues in amine uni...
The common industrial practice of using aqueous solutions of diethanolamine (DEA) for the removal of...
Alkanolamine solutions and glycol solutions present operational problems while performing vital gas ...
Enhanced oil and gas recovery is often performed with seawater injection in the well as pressure com...
The benefits of reclaiming amine systems are trumpeted by many and doubted by others. Removing the c...
Flue gas desulfurisation is a prerequisite for successful CO2 capture in coal-fired power stations u...
are unable to remove COS from syngas and off-gas streams, and HCN causes severe degradation of the a...
AbstractHeat-stable salts (HSS) in amine-based solvents may lead to a long-term performance impairme...
This paper includes the significant on-site experience of the authors related to problems faced in a...
Monoethylene glycol (MEG), a common hydrate inhibitor in natural gas transportation pipelines is usu...
Abstract The gas sweetening unit of phase 2 and 3 in South Pars Gas Field (Asalouyeh, Iran) was firs...
International audienceIn the oil and gas industry, acid gas removal is required for the treatment of...
"""sour"" natural gases are ""sweetened"" by reaction with alkaline solutions to remove H2S, CO, and...
International audienceProcesses using amine solvents for the removal of CO 2 have long been used for...
Amines are used in refineries and gas plants around the world to remove both H2S and CO2 from feed g...
International audienceCorrosion represents one of the most important operational issues in amine uni...
The common industrial practice of using aqueous solutions of diethanolamine (DEA) for the removal of...
Alkanolamine solutions and glycol solutions present operational problems while performing vital gas ...
Enhanced oil and gas recovery is often performed with seawater injection in the well as pressure com...
The benefits of reclaiming amine systems are trumpeted by many and doubted by others. Removing the c...
Flue gas desulfurisation is a prerequisite for successful CO2 capture in coal-fired power stations u...
are unable to remove COS from syngas and off-gas streams, and HCN causes severe degradation of the a...
AbstractHeat-stable salts (HSS) in amine-based solvents may lead to a long-term performance impairme...
This paper includes the significant on-site experience of the authors related to problems faced in a...
Monoethylene glycol (MEG), a common hydrate inhibitor in natural gas transportation pipelines is usu...
Abstract The gas sweetening unit of phase 2 and 3 in South Pars Gas Field (Asalouyeh, Iran) was firs...