Method of absorbing acid compounds contained in a gaseous effluent using an amine-based aqueous solution

Patent metadata

Field	Value
Publication number	US-10137404-B2
Application number	US-201313975620-A
Country	US
Kind code	B2
Filing date	Aug 26, 2013
Priority date	Aug 30, 2012
Publication date	Nov 27, 2018
Grant date	Nov 27, 2018

Abstract

The gaseous effluent is contacted with an aqueous solution comprising at least one amine and at least one amine degradation inhibiting compound. A stainless steel withstanding corrosion upon contact with the amine degradation inhibiting compound is first selected. Equipments whose surfaces in contact with the aqueous solution are made from this stainless steel are used.

First claim

The invention claimed is:

1. A method of absorbing acid compounds contained in a gaseous effluent comprising the following stages:
contacting the gaseous effluent with an aqueous solution comprising at least one amine and at least one amine degradation inhibiting compound,
determining a corrosion resistance of each of a plurality of stainless steels of grades 1.4462 or 1.4410 or 1.4547 upon contact with a triazole or tetrazole derivative comprising at least one substituent having a sulfur atom,
selecting a stainless steel of grade 1.4462 or 1.4410 or 1.4547 based on the determination of the corrosion resistances of the plurality of stainless, and
using equipments whose surfaces in contact with said aqueous solution are made from the selected stainless steel.

2. A method as claimed in claim 1 , wherein the stage of selecting a stainless steel based on the determination of the corrosion resistances of the plurality of stainless steels comprises selecting a stainless steel having the lowest corrosion rate among the plurality of stainless steels, said lowest corrosion rate being determined in the presence of said degradation inhibiting compound.

3. A method as claimed in claim 2 , wherein the stage of selecting a stainless steel based on the determination of the corrosion resistances of the plurality of stainless steels comprises selecting a stainless steel based on the determination of the relative corrosion resistances of a plurality of stainless steels upon contact with said amine degradation inhibiting compound at a temperature of said aqueous solution in contact with said stainless steel.

4. A method as claimed in claim 1 , wherein a stainless steel comprising:
at most 0.03% C,
at least 18% and up to 28% Cr,
at least 2% and up to 8% Mo,
at least 0.08% and up to 0.5% N,
less than 31% Ni

is used.

5. A method as claimed in claim 4 , wherein a stainless steel of Duplex or Super Duplex type is used.

6. A method as claimed in claim 3 , wherein, the temperature of said aqueous solution in contact with said stainless steel is below 90° C., and a stainless steel comprising:
at most 0.03% C,
at least 18% and up to 28% Cr,
at least 2% and up to 5% Mo,
at least 0.1% and up to 0.3% N,
less than 20% Ni

is used.

7. A method as claimed in claim 3 wherein, the temperature of said aqueous solution in contact with said stainless steel is above 90° C., and a stainless steel comprising:
at most 0.03% C,
at least 20% and up to 28% Cr,
at least 2.5% and up to 8% Mo,
at least 0.1% and up to 0.5% N,
less than 31% Ni

is used.

8. A method as claimed in claim 1 , wherein the aqueous amine solution comprises between 10 wt. % and 80 wt. % of amines selected from the list consisting of monoethanolamine (MEA), diethanolamine, dimethylethanolamine, diisopropylamine, diglycolamine, piperazine, hydroxyethyl piperazine, 1,3-Bis(dimethylamino)-2-propanol, 1,3-Bis(methyl-ethylamino)-2-propanol, 1,3-Bis(ethylamino)-2-propanol, 1,3-Bis(diethylamino)-2-propanol, 1,3-bis(methylamino)-2-propanol, 1,3 Bis(npropylamino)-2-propanol, 1,3-Bis(isopropylamino)-2-propanol, 1,3 Bis(nbutylamino)-2-propanol, 1,3-Bis(isobutylamino)-2-propanol, 1,3 Bis(terbutylamino)-2-propanol, 1,3-Bis[(2-hydroxyethyl)methylamino]-2-propanol, 1,3-Bis(piperidino)-2-propanol, and 1,3-Bis(pyrrolidino)-2-propanol.

9. A method as claimed in claim 8 , wherein the aqueous solution comprises between 30 wt. % and 50 wt. % monoethanolamine (MEA).

10. A method as claimed in claim 1 , wherein said degradation inhibiting compound meets one of the following general formulas:

wherein radical R 1 is selected from among:
a hydrogen atom,
a hydrocarbon radical comprising 1 to 12 carbon atoms,
an amino radical of general formula —NR 4 R 5 wherein radical R 4 and radical R 5 are independently selected from among:
a hydrogen atom,
a hydrocarbon radical comprising 1 to 12 carbon atoms,

and wherein each radical R 2 and R 3 is independently selected from among the following elements:
a) —S—X wherein radical X is selected from among:
a hydrogen atom,
an alkaline or alkaline-earth element,
a monovalent or multivalent metal,
an ammonium cation NH4+ or resulting from the protonation of an amine function,
a phosphonium cation,
a hydrocarbon radical comprising 1 to 12 carbon atoms,
a radical selected from among a thiyl-triazole, thio-triazole, thiyl-tetrazole and thio-tetrazole radical,

b) a hydrogen atom,
c) a hydroxyl radical,
d) an amino radical of general formula —NR 4 R 5 wherein radical R 4 and radical R 5 are independently selected from among:
a hydrogen atom,
a hydrocarbon radical comprising 1 to 12 carbon atoms,

e) a radical comprising 1 to 12 carbon atoms.

11. A method as claimed in claim 1 , wherein the degradation inhibiting compound is selected from the group containing: 1H-1,2,4-triazole-3-thiol, a 1H-1,2,4-triazole-3-thiol salt, 5-phenyl-1H-1,2,4-triazole-3-thiol, a 5-phenyl-1H-1,2,4-triazole-3-thiol salt, 5-(4-pyridyl)-1H-1,2,4-triazole-3-thiol, a 5-(4-pyridyl)-1H-1,2,4-triazole-3-thiol salt, 5-(3-pyridyl)-1H-1,2,4-triazole-3-thiol, a 5-(3-pyridyl)-1H-1,2,4-triazole-3-thiol salt, 4-methyl-4H-1,2,4-triazole-3-thiol, a 4-methyl-4H-1,2,4-triazole-3-thiol salt, 4-methyl-5-(2-thienyl)-4H-1,2,4-triazole-3-thiol, a 4-methyl-5-(2-thienyl)-4H-1,2,4-triazole-3-thiol salt, 4-methyl-5-(3-thienylmethyl)-4H-1,2,4-triazole-3-thiol, a 4-methyl-5-(3-thienylmethyl)-4H-1,2,4-triazole-3-thiol salt, 4-cyclohexyl-5-sulfanyl-4H-1,2,4-triazole-3-ol, a 4-cyclohexyl-5-sulfanyl-4H-1,2,4-triazole-3-ol salt, 3-amino-1,2,4-triazole-5-thiol, a 3-amino-1,2,4-triazole-5-thiol salt, 4-amino-4H-1,2,4-triazole-3,5-dithiol, a 4-amino-4H-1,2,4-triazole-3,5-dithiol salt, [1,2,4] triazolo[4,3-a]pyridine-3-thiol, a [1,2,4]triazolo[4,3-a]pyridine-3-thiol salt, 1H-5-mercapto-1,2,3-triazole, a 1H-5-mercapto-1,2,3-triazole salt, 1-methyl-1H-tetrazole-5-thiol, a 1-methyl-1H-tetrazole-5-thiol salt, 1-ethyl-1H-tetrazole-5-thiol, a 1-ethyl-1H-tetrazole-5-thiol salt, 1-phenyl-1H-tetrazole-5-thiol, a 1-phenyl-1H-tetrazole-5-thiol salt, 1-(4-hydroxy-phenyl)-1H-tetrazole-5-thiol, a 1-(4-hydroxyphenyl)-1H-tetrazole-5-thiol salt, 5-mercapto-1-tetrazolacetic acid, a 5-mercapto-1-tetrazolacetic acid salt, 1-[2-(dimethyl-amino)ethyl]-1H-tetrazole-5-thiol, a 1-[2-(dimethylamino)ethyl]-1H-tetrazole-5-thiol salt, 3-amino-5-methylthio-1H-1,2,4-triazole, a 3-amino-5-methylthio-1H-1,2,4-triazole salt, 5-(methylthio)-1H-tetrazole, a 5-(methylthio)-1H-tetrazole salt, 5-(ethylthio)-1H-tetrazole, a 5-(ethylthio)-1H-tetrazole salt, 1-methyl-5-(methylthio)-1H-tetrazole, a 1-methyl-5-(methylthio)-1H-tetrazole salt, 4-phenyl-4H-1,2,4-triazole-3-thiol, a 4-phenyl-4H-1,2,4-triazole-3-thiol salt, 5-methyl-4H-1,2,4-triazole-3-thiol, a 5-methyl-4H-1,2,4-triazole-3-thiol salt, 5-(trifluoromethyl)-2,4-dihydro-3H-1,2,4-triazole-3-thione, a 5-(trifluoromethyl)-2,4-dihydro-3H-1,2,4-triazole-3-thione salt, 4-isopropyl-4H-1,2,4-triazole-3-thiol and a 4-isopropyl-4H-1,2,4-triazole-3-thiol salt.

12. A method as claimed in claim 1 , wherein the acid compounds belong to a group comprising CO 2 and H 2 S.

13. A method as claimed in claim 1 , wherein the method is implemented for absorbing acid compounds contained in one of the effluents of the group consisting of natural gas, combustion fumes, syngas, refinery gas, Claus tail gases, biomass fermentation gases, cement plant gases and incinerator fumes.

14. A method as claimed in claim 1 , wherein the stage of s

Assignees

• Ifp Energies Now

Inventors

• Kittel Jean
• Gonzalez Serge
• Lemaire Eric
• Bonneau Alexandre

Classifications

• B01D2257/504

  Carbon dioxide · CPC title

• B01D53/18

  Absorbing units; Liquid distributors therefor (B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32) · CPC title

• B01D2252/20489

  with two or more hydroxyl groups · CPC title

• B01D2258/0233

  from cement factories · CPC title

• B01D2252/604

  Stabilisers or agents inhibiting degradation · CPC title