Absorbent and process for selectively removing hydrogen sulfide
US-2020164303-A1 · May 28, 2020 · US
US11045759B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11045759-B2 |
| Application number | US-201716093731-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 6, 2017 |
| Priority date | Apr 18, 2016 |
| Publication date | Jun 29, 2021 |
| Grant date | Jun 29, 2021 |
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A premixture for producing an absorbent for removing acid gases from a fluid stream containing a) at least a tertiary amine and/or a sterically hindered secondary amine; b) a dicarboxylic acid in an amount, calculated as neutralization equivalent based on the protonatable nitrogen atoms in a), of at least 30%, wherein the dicarboxylic acid has a solubility in water at a temperature of 20° C. of not more than 15 g of dicarboxylic acid per 100 g of water; and c) 20 to 80 wt % of water. Also described is a process for producing an absorbent from the premixture. The premixture is a transportable and readily handleable solution of a dicarboxylic acid having poor solubility in water for producing an absorbent for removing acid gases from a fluid stream.
Opening claim text (preview).
The invention claimed is: 1. A premixture, comprising a) a tertiary amine which is at least one alkanolamine selected from bis(2-hydroxyethyl)methylamine, tributanolamine, 2-diethylaminoethanol, 2-dimethylaminoethanol, 3-dimethylamino-1-propanol, 3-diethylamino-1-propanol, 2-diisopropylaminoethanol, and N,N-bis(2-hydroxypropyl)methylamine; b) a dicarboxylic acid in an amount, calculated as neutralization equivalent based on protonatable nitrogen atoms in the tertiary amine, of at least 30%, wherein the dicarboxylic acid has a solubility in water at a temperature of 20° C. of not more than 15 g of dicarboxylic acid per 100 g of water; and c) from 20 to 80 wt % of water, wherein the premixture is suitable for producing an absorbent for removing acid gases from a fluid stream, and wherein the dicarboxylic acid is at least one selected from the group consisting of succinic acid, adipic acid, pimelic acid, suberic acid, azelaic acid, and sebacic acid. 2. The premixture according to claim 1 , wherein the amount of the dicarboxylic acid, calculated as neutralization equivalent based on the protonatable nitrogen atoms in a), is from 30% to 400%. 3. The premixture according to claim 1 , wherein the dicarboxylic acid is selected from the group consisting of succinic acid and adipic acid. 4. A process for producing an absorbent for removing acid gases from a fluid stream, the process comprising: mixing the premixture of claim 1 with an amine and optionally with water, wherein the amount of the dicarboxylic acid in the premixture, calculated as neutralization equivalent based on the protonatable nitrogen atoms of the tertiary amine, is greater than in the absorbent. 5. The process of claim 4 , wherein the absorbent comprises the dicarboxylic acid in an amount, calculated as neutralization equivalent based on the protonatable nitrogen atoms of the tertiary amine, of from 0.5% to 15%. 6. The process of claim 4 , wherein the absorbent is free from sterically unhindered primary amines and sterically unhindered secondary amines.
of CO2 · CPC title
Flue gases · CPC title
Mixtures of two or more absorbents · CPC title
Alkanolamines · CPC title
Removing carbon dioxide · CPC title
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