US2015151240A1PendingUtilityA1

Aqueous absorbent composition for enhanced removal of hydrogen sulfide from gaseous mixtures and method for using the same

Assignee: DOW GLOBAL TECHNOLOGIES LLCPriority: Jun 29, 2012Filed: Jun 6, 2013Published: Jun 4, 2015
Est. expiryJun 29, 2032(~5.9 yrs left)· nominal 20-yr term from priority
B01D 53/1462B01D 2252/20489B01D 53/1493B01D 2252/20447Y02C20/40C10L 2290/545C10L 2290/541C10L 2290/12C10L 3/103C10L 3/10C10K 1/143C10K 1/004C10G 70/00C10G 29/20C10G 21/20C07C 7/11B01D 2252/504B01D 2252/20431B01D 2252/20426B01D 2252/2041B01D 2252/20405B01D 2252/103B01D 53/52B01D 53/1468B01D 53/14B01D 2252/20484C10L 3/102C10K 1/005B01D 2252/2025B01D 2252/2023B01D 53/1425B01D 2252/20421C10L 3/104C10K 1/003
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Claims

Abstract

The present invention relates to an aqueous alkanolamine solution for the removal of hydrogen sulfide from gaseous mixtures containing hydrogen sulfide. The aqueous alkanolamine solution comprises (i) an amino compound with the formula: R 1 R 2 NCH 2 CH(OH)CH 2 OH wherein R 1 and R 2 independently represent lower alkyl groups of 1 to 3 carbon atoms, (ii) piperazine, and (iii) optionally a physical solvent, wherein said solution does not contain a strong acid. Further, the present invention relates to a process for removing hydrogen sulfide from a gaseous mixture containing hydrogen sulfide, and additionally other acid gases, if present, for example carbon dioxide, comprising the step of contacting the gaseous mixture contain hydrogen sulfide with the aqueous alkanolamine solution, preferably wherein the temperature of the aqueous alkanolamine solution is equal to or greater than 140° F. Examples of the gaseous mixtures include natural gas, synthesis gas, tail gas, and refinery gas.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . An aqueous alkanolamine solution for the removal of acid gasses including hydrogen sulfide from gas mixtures containing hydrogen sulfide comprising:
 (i) an amino compound with the formula:
   R 1 R 2 NCH 2 CH(OH)CH 2 OH 
   wherein R 1  and R 2  independently represent methyl, ethyl, propyl, or isopropyl groups,   and   (ii) piperazine,   
       wherein said aqueous alkanolamine solution does not contain an acid having a pKa of 8 or less or an acid-forming material capable of forming in aqueous medium an acid having a pKa of 8 or less. 
     
     
         2 . The aqueous alkanolamine solution of  claim 1  wherein
 (i) the amino compound is present in an amount of from 0.1 to 75 weight percent, 
 and 
 (ii) the piperazine is present in an amount of from 0.1 to 15 weight percent, 
 
       wherein weight percent is based on the total weight of the aqueous alkanolamine solution. 
     
     
         3 . The aqueous alkanolamine solution of  claim 1  wherein the amino compound (i) is 3-(dimethylamino)-1,2-propanediol or 3-(diethylamino)-1,2-propanediol. 
     
     
         4 . The aqueous alkanolamine solution of  claim 1  further comprises (iii) a physical solvent. 
     
     
         5 . The aqueous alkanolamine solution of  claim 4  wherein the physical solvent (iii) is selected from cyclotetramethylenesulfone, dimethyl ethers of polyethylene glycol, 1,3-dimethyl-3,4,5,6-tetrahydro-2(1H)-pyrimidinone, N-formylmorpholine, N-acetylmorpholine, triethylene glycol monomethyl ether, or mixtures thereof. 
     
     
         6 . A process for removing acid gases from a gaseous mixture comprising the step of contacting the gaseous mixture with the aqueous alkanolamine solution of any of the  claims 1  to  3 . 
     
     
         7 . The process of  claim 6  further comprising the step of steam stripping the aqueous alkanolamine solution such that an acid gas-lean aqueous alkanolamine solution is formed which may be used in said contacting step. 
     
     
         8 . The process of  claim 6  wherein the temperature of the aqueous alkanolamine solution is equal to or greater than 140° F.

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