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An aqueous co2 absorbent comprising 2-amino-2-methyl-1-propanol and 3-aminopropanol or 2-amino-2-methyl-1-propanol and 4-aminobutanol

a technology of aqueous co2 and aqueous amine, which is applied in the direction of separation processes, hydrogen sulfides, sulfur compounds, etc., can solve the problems of reducing increasing the operating cost of co2 plants, and increasing so as to improve the oxidative degradation rate of amines and reduce the corrosive

Inactive Publication Date: 2015-10-29
AKER SOLUTIONS AS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The patent text discusses the use of a new absorbent called CO2-AMP-AP or CO2-AMP-AB, which is better at absorbing CO2 than traditional absorbents like MEA. The new absorbent is also less prone to degradation and corrosive to plant parts, which means it has a longer lifespan and is safer to use in industry. This is because the absorbent contains a combination of AMP and AP or AMP and AB, which helps to reduce the amount of ions that are released into the absorbent. These ions can cause degradation of the absorbent and lead to high operating costs. The new absorbent is also less corrosive, which means it is safer for use in industrial applications.

Problems solved by technology

Capture of CO2 is, however, an energy demanding process, as the binding of CO2 to the absorbent is an exothermal reaction and the regeneration is an endothermal reaction.
This heat demand is a major operating cost for a plant for CO2 capture.
Amines are also prone to degradation and are corrosive in the environment where they are used.
Degradation is unwanted, both as degradation inactivates the absorbent and causes a need for make-up filling of amine into the plant, as potentially large amounts of waste products are produced, and as the long term operation will be more dependent of a reclaimer unit to recover usable amines bound to degradation products (so called Heat Stable Amine Salts).
This implies a risk for emissions of volatile amine components or degradation products to the environment.
Nitrosamines formation is limited by avoiding the use of secondary amines and by limiting solvent degradation.
Corrosion is of concern both as it is detrimental for important parts of the plant and may reduce the life expectancy thereof, or cause a requirement for more expensive construction elements, and as products of corrosion, such as Fe-ions, may be detrimental to the absorbent by causing higher degree of degradation.

Method used

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  • An aqueous co2 absorbent comprising 2-amino-2-methyl-1-propanol and 3-aminopropanol or 2-amino-2-methyl-1-propanol and 4-aminobutanol
  • An aqueous co2 absorbent comprising 2-amino-2-methyl-1-propanol and 3-aminopropanol or 2-amino-2-methyl-1-propanol and 4-aminobutanol
  • An aqueous co2 absorbent comprising 2-amino-2-methyl-1-propanol and 3-aminopropanol or 2-amino-2-methyl-1-propanol and 4-aminobutanol

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Embodiment Construction

[0038]The present invention relates to an improved amine absorbent for CO2 capture and a method for capturing CO2 using the improved amine absorbent.

[0039]The invention is based on mixing two different primary amines having different reaction kinetics, one being a sterically hindered amine, namely 2-amino-2-methyl-1-propanol (AMP) and the other being a monoalkanolamine, namely 3-aminopropanol (AP), or 4-aminobutanol (AB).

[0040]AMP, being a sterically hindered amine, is known to have low energy requirement for regeneration of the absorbent but the slow reaction kinetics have a negative impact in the absorber as it requires a longer contact time between the CO2 containing gas and the absorbent in the absorber. As opposed to the reference amine, MEA, commonly used in 30 wt %, corresponding to a molar concentration of 5 mol / l, AMP cannot be used alone in higher concentrations than about 4 mol / l, corresponding to about 35% by weight, due to precipitation formed upon reaction with CO2. Th...

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Abstract

An aqueous CO2 absorbent comprising a combination of 2-amino-2-methyl-1-propanol (AMP) and 3-aminopropanol (AP), or AMP and 4-aminobutanol (AB), is described. A method for capturing CO2 from a CO2 containing gas using the mentioned absorbent, and the use of a combination of AMP and AP, or a combination of AMP and AB are also described.

Description

TECHNICAL FIELD[0001]The present invention relates to an improved method for capturing of CO2 from a combustion gas, and to an improved amine absorbent for CO2.BACKGROUND ART[0002]Capture of CO2 from a mixture of gases in an industrial scale has been known for decades, i.e. for separation of natural gas and CO2 from sub terrain gas wells to give natural gas for export and CO2 for return to the sub terrain structure.[0003]The growing concern on environment and the greenhouse effect of CO2 from combustion of fossil fuels has caused a growing interest in CO2 capture from major points of emission of CO2 such as thermal power plants, in so called Post Combustion CO2 capture[0004]Even if power plants represent the largest point sources for CO2 emissions, other industries like steelworks and cement plants can utilize similar technologies for CO2 capture.[0005]U.S. Pat. No. 5,618,506, and EP 0 558 019, both to The Kansai Electric Power Co., Inc., and Mitsubishi Jukogyo Kabushiki Kaisha, and...

Claims

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Application Information

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IPC IPC(8): B01D53/14C01B32/50
CPCB01D53/1475B01D53/1493B01D2252/20421B01D2252/20405B01D2252/504B01D2258/0283B01D2252/20484Y02C20/40
Inventor HOFF, KARL ANDERSMEJDELL, THORKIM, INNAGRIMSTVEDT, ANDREASDA SILVA, EIRIK FALCK
Owner AKER SOLUTIONS AS
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