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Absorbing solvent for capturing or separating carbon dioxide from gas mixture or liquid gas

A gas mixture and solvent absorption technology, applied in the direction of absorption, carbon compounds, separation methods, etc., can solve the problems of high degradation and high cost of use, and achieve the effects of improving solubility and desorption, improving stability, and reducing degradation loss

Inactive Publication Date: 2008-10-08
TSINGHUA UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the special structure of these hindered amines, the degradation during use is relatively large, and the cost of use is still high

Method used

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  • Absorbing solvent for capturing or separating carbon dioxide from gas mixture or liquid gas
  • Absorbing solvent for capturing or separating carbon dioxide from gas mixture or liquid gas
  • Absorbing solvent for capturing or separating carbon dioxide from gas mixture or liquid gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] Get three parts of the n-propanolamine aqueous solution that the n-propanolamine content is 5wt%, the temperature is 40 ℃, gas phase CO 2 Partial pressure of 5kPa, 50kPa, 120kPa containing CO 2 and N 2 The mixed gas of the mixed gas is input into three parts of the solvent respectively, and after the gas-liquid two-phase reaches equilibrium, the CO in the solvent is absorbed 2 and the molar ratio of n-propanolamine (MPA) and CO in the absorption solvent 2 See Table 1 for the solubility.

[0015] Table 1 Experimental results of n-propanolamine aqueous solution at 40°C and 5wt%

[0016]

Embodiment 2

[0018] Get three parts of the n-propanolamine aqueous solution that the n-propanolamine content is 5wt%, the temperature is 120 ℃, gas phase CO 2 Partial pressure of 21kPa, 90kPa, 150kPa containing CO 2 and N 2 The mixed gas of the mixed gas is input into three parts of the solvent respectively, and after the gas-liquid two-phase reaches equilibrium, the CO in the solvent is absorbed 2 and the molar ratio of n-propanolamine (MPA) and CO in the absorption solvent 2 See Table 2 for the solubility.

[0019] Table 2 Experimental results of 120°C, 5wt% n-propanolamine aqueous solution

[0020]

Embodiment 3

[0022] Get three parts of n-propanolamine aqueous solution that n-propanolamine content is 15wt%, the temperature is 40 ℃, gas phase CO 2 Partial pressure of 4kPa, 49kPa, 128kPa containing CO 2 and N 2 The mixed gas of the mixed gas is input into three parts of the solvent respectively, and after the gas-liquid two-phase reaches equilibrium, the CO in the solvent is absorbed 2 and the molar ratio of n-propanolamine (MPA) and CO in the absorption solvent 2 See Table 3 for the solubility.

[0023] Table 3 Experimental results of n-propanolamine aqueous solution at 40°C and 15wt%

[0024]

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PUM

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Abstract

The invention pertains to the field of chemical materials and in particular relates to a sorption solvent which catches or separates carbon dioxide from gaseous mixtures or liquefied gases. The solvent comprises n-propanolamine with a content range of 5-60wt% and other components with a total content range of 40-95wt%; other components comprise monoethanol amine, diethanolamine, methyl diethanolamine, diisopropanol amine, 2-amido-2-methyl-1-propyl alcohol, organic amine, water, physical solvent, inorganic salt and one or more accessory ingredients. The number of carbon atoms between the amidocyanogen and the hydroxide radical of the n-propanolamine is three; nitrogen atoms can form a hydrogen bond with the hydrogen atoms on oxygen atoms, or oxygen atoms can form a hydrogen bond with the hydrogen atoms on nitrogen atoms, thus forming a ring structure composed of six atoms; such molecular structure is similar to that of secondary amine, can reduce the formation of amino carbonates and improve the solubility and desorption degree of CO2; meanwhile, the formation of the six-element ring molecular structure increases the stability of molecular and can reduce the degradation loss of solvents in service process.

Description

technical field [0001] The invention belongs to the field of chemical materials, in particular to a method for capturing or separating carbon dioxide (CO2) from gas mixtures or liquefied gases. 2 ) of the absorbing solvent. Background technique [0002] CO 2 Emissions of greenhouse gases such as greenhouse gases are a major factor causing climate change, how to enrich CO 2 capture or separation of CO in a gas mixture or liquefied gas 2 becomes extremely important. These gas mixtures include flue gas, refinery gas, natural gas, liquefied gas, synthesis gas, shift gas and hydrogen production gas, among others. The gas mixture contains 5% to 80% CO 2 , other major gas components include N 2 , O 2 , CO, H 2 、CH 4 、C 2 h 6 , SO 2 、H 2 S and organic sulfur CH 3 S, COS, etc.; the pressure range of the gas is large (50-9000kPa), suitable for capturing and separating CO by chemical absorption or chemical-physical composite absorption 2 components. [0003] At present,...

Claims

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Application Information

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IPC IPC(8): B01D53/14C01B31/20C01B32/50
CPCY02C10/06Y02C20/40Y02P20/151
Inventor 陈健董立户高光华
Owner TSINGHUA UNIV
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