Removal of acid gases from a fluid flow by means of reduced coabsorption of hydrocarbons and oxygen
A process for removing acid gases from a hydrocarbonaceous fluid stream or an oxygen-comprising fluid stream in which the fluid stream is contacted with an aqueous solution which is essentially free from inorganic basic salts and comprises (i) at least one amine and (ii) at least one metal salt of an aminocarboxylic acid and/or an aminosulfonic acid. Conjoint use of the aminocarboxylic and/or aminosulfonic salt reduces the coabsorption of hydrocarbons or oxygen without significantly impairing the absorption rate at which acid gases are absorbed, without significantly reducing the absorption capacity of the solution for acid gases, and without significantly increasing the energy demand required for regeneration.
1. A process for removing acid gases from a hydrocarbonaceous fluid stream which comprises
contacting the fluid stream with an aqueous solution which is essentially free from inorganic basic salts and comprises
(i) 2 to 5 kmol/m 3 of methyldiethanolamine, and
(ii) 0.5 to 2 kmol/m 3 of at least one metal salt of an aminocarboxylic acid, at least one metal salt of an aminosulfonic acid, or a mixture of at least one metal salt of an aminocarboxylic acid and at least one metal salt of an aminosulfonic acid,
wherein the overall pressure while contacting the fluid stream with aqueous solution is 10 to 100 bar.
2. The process according to claim 1 , wherein the aminocarboxylic acid is an α-amino acid or a β-amino acid and the aminosulfonic acid is an α-aminosulfonic acid or a β-aminosulfonic acid.
3. The process according to claim 1 , in which the metal salt is an alkali metal or alkaline earth metal salt.
4. The process according to claim 1 , wherein the metal salt of the aminocarboxylic acid is the potassium salt of N,N-dimethylglycine or N-methylalanine.
5. The process according to claim 1 , wherein component (ii) is 0.5 to 2 kmol/m 3 of at least one metal salt of an aminosulfonic acid.
6. The process according to claim 1 , wherein component (ii) is 0.5 to 2 kmol/m 3 of a mixture of at least one metal salt of an amino carboxylic acid and at least one metal salt of an aminosulfonic acid.
7. The process according to claim 1 , wherein the aminocarboxylic acid is a N-mono-C 1 -C 4 -alkylaminocarboxylic acid or a N,N-di-C 1 -C 4 -alkylaminocarboxylic acid.
8. The process according to claim 7 , wherein the metal salt of the aminocarboxylic acid is the potassium salt of N,N-dimethylglycine or N-methylalanine.
9. The process according to claim 1 , in which the aqueous solution in addition comprises one or more activators.
10. The process according to claim 9 , wherein the activator is selected from the group consisting of piperazine, methylaminopropylamine, aminoethoxyethanol and 2-amino-1-butanol.
11. The process according to claim 10 , wherein the aqueous solution comprises methyldiethanolamine and piperazine.
12. The process according to claim 10 , wherein the aqueous solution comprises:
(i) methyldiethanolamine and methylaminopropylamine,
(ii) methyldiethanolamine and aminoethoxyethanol, or
(iii) methyldiethanolamine and 2-amino-1-butanol.