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Carbon dioxide absorber and carbon dioxide separation/recovery method using the absorber

a carbon dioxide and absorber technology, applied in the direction of hydrogen sulfides, separation processes, energy input, etc., can solve the problems of difficult to save energy, serious economic shortcomings, and inability to know the chemical properties of absorption of carbon dioxide, so as to prevent volatilization of amine compounds and metal corrosion, reduce the effect of oxidation

Inactive Publication Date: 2016-07-07
ASAHI KASEI KK
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The present invention provides a carbon dioxide absorber and a method for separating and recovering carbon dioxide from gas. The carbon dioxide absorber can efficiently and stably remove carbon dioxide from gas or solution. It prevents corrosion of metal and volatilization of amine compounds. The carbon dioxide absorber is stable and can be used for a long time. The carbon dioxide removal method and separation / recovery method are efficient during continuous use. The carbon dioxide absorber and the carbon dioxide separation / recovery method are stable and can be used repeatedly.

Problems solved by technology

Since conventional technologies for separating and recovering carbon dioxide, such as a chemical absorption process, require a large amount of additional energy for separating carbon dioxide from absorbers, they have extremely serious economic shortcomings.
However, since alkaline metals are strongly basic, it has been difficult to save energy despite the strong acidity of acidic compounds.
However, since this is used only as an intermediate substance for forming a cosmetic compound, its chemical properties relating to absorption of carbon dioxide are not known.
However, although this use of a heat pump achieves a certain degree of energy savings, when the equipment costs of this system are taken into consideration, the effects cannot be said to be adequate.
In this apparatus as well, the thermal energy able to be used from the flue gas is unable to achieve adequate energy savings.

Method used

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  • Carbon dioxide absorber and carbon dioxide separation/recovery method using the absorber
  • Carbon dioxide absorber and carbon dioxide separation/recovery method using the absorber
  • Carbon dioxide absorber and carbon dioxide separation/recovery method using the absorber

Examples

Experimental program
Comparison scheme
Effect test

examples

[0182]The following provides a more detailed explanation of the present invention through examples thereof. Furthermore, the present invention is not limited by the following examples.

[0183]

[0184]MEA: Monoethanolamine

[0185]DEA: Diethanolamine

[0186]Pz: Piperazine

[0187]MDEA: Methyldiethanolamine

[0188]BHEP: 1,3-bis(2-hydroxyethylamino)propan-2-ol

[0189]BHPP: 1,3-bis(2-hydroxypropylamino)propan-2-ol

[0190]HEHPP: 1-(2-hydroxyethylamino)-3-(2-hydroxypropylamino)propan-2-ol

[0191]DAP: 1,3-diaminopropan-2-ol

[0192]THPP: 1,3-tetrakis(2-hydroxypropylamino)propan-2-ol

[0193]EAE: 2-ethylaminoethanol

[0194]2A13PD: 2-amino-1,3-propanediol

[0195]IPAE: 2-isopropylaminoethanol

[0196]TMB: Trimethylborate

[0197]TEB: Triethylborate

Carbon Dioxide Absorber of First Configuration

examples 1 to 4

[0198]In order to evaluate the first configuration of the present invention, an amine compound, a weakly acidic compound and water were mixed and dissolved in the ratios shown in Table 1 to obtain carbon dioxide absorbers. The pKb values of the amine compounds, the pKa values of the weakly acidic compounds, and the number of equivalents of the weakly acidic compounds with respect to amino groups are shown in Table 1. The pKb values of the amine compounds and the pKa values of the weakly acidic compounds were respectively calculated from the pH value in a 0.4 M aqueous solution.

TABLE 1WeaklyEq / no.WaterAmineWtacidicWtof aminocontentcompoundpKb%compoundpKa%groups(wt %)Ex. 1MEA4.728.3Boric acid9.25.70.266.0Ex. 2MEA4.723.0Boric acid9.223.31.053.7Ex. 3DEA5.447.2Boric acid9.25.60.247.2Ex. 4DEA5.445.6Boric acid9.22.30.07*148.9Pz4.83.2Ex. 5Pz4.821.2Boric acid9.215.20.563.6Comp. Ex. 1MEA4.728.3Acetic acid4.85.60.266.1Comp. Ex. 2MEA4.730.0None———70.0Comp. Ex. 3DEA5.450.0None———50.0Comp. Ex. 4D...

examples 6 to 12

[0222]In order to evaluate the first configuration of the present invention, an amine compound, a weakly acidic compound and water were mixed and dissolved in the ratios shown in Table 4 to obtain carbon dioxide absorbers. The results of testing these absorbers in the same manner as the absorbers of Examples 3 and 4 and Comparative Examples 3 to 5 are shown in Table 5.

TABLE 4WeaklyEq / no.WaterAmineWtacidicWtof aminocontentcompoundpKb%compoundpKa%groups(wt %)Ex. 6EAE4.444.0Boric acid9.230.153.0Ex. 72A13PD5.645.0Boric acid9.230.152.0Ex. 8IPAE4.150.0Boric acid9.230.147.0Ex. 9IPAE4.145.5Boric acid9.23.50.1*246.5Pz4.846.6Ex. 10MDEA5.746.6Boric acid9.22.50.08*347.5Pz4.83.4Ex. 11DEA5.450.0TMB8.74.80.0945.2Ex. 12DEA5.450.0TEB8.16.80.0943.2Comp. Ex. 7EAE4.444.0None———56.0Comp. Ex. 82A13PD5.645.0None———55.0Comp. Ex. 9IPAE4.150.0None———50.0Comp. Ex. 10IPAE4.145.5None———50.0Pz4.84.5Comp. Ex. 11MDEA5.746.6None———50.0Pz4.83.4*20.9 equivalents when converted based on 1 mole of piperazine*31.0 equiv...

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Abstract

The present invention provides a carbon dioxide absorber capable of efficiently and stably removing carbon dioxide in a gas or solution. This carbon dioxide absorber contains an amine compound, a weakly acidic compound and water, the pKb value of the amine compound in an aqueous solution at 30° C. is 4.0 to 7.0, the pKa value of the weakly acidic compound in an aqueous solution at 30° C. is 7.0 to 10.0, and the weakly acidic compound is present in an amount within the range of 0.01 equivalents to 1.50 equivalents with respect to amino groups of the amine compound.

Description

[0001]This application is a Divisional of copending application Ser. No. 14 / 125,048, filed on Dec. 9, 2013, which was filed as PCT International Application No. PCT / JP2012 / 064843 on Jun. 8, 2012, which claims the benefit under 35 U.S.C. §119(a) to Patent Application No. JP 2011-129327, filed in Japan on Jun. 9, 2011, Patent Application No. JP 2011-129438, filed in Japan on Jun. 9, 2011, and Patent Application No. JP 2011-171263, filed in Japan on Aug. 4, 2011, all of which are hereby expressly incorporated by reference into the present application.[0002]The present invention relates to a carbon dioxide absorber for absorbing and removing carbon dioxide contained in a gas, and more particularly, to a carbon dioxide absorber which can separate and recover carbon dioxide from a gas while saving energy. In addition, the present invention relates to a method for separating and recovering carbon dioxide from a gas containing carbon dioxide, such as combustion exhaust gas. Moreover, the pr...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B01D53/78B01D53/62B01D53/14C01B32/50
CPCB01D53/78B01D53/1493B01D53/1475B01D2258/0283B01D53/62B01D2252/20426B01D2257/504B01D53/1425B01D2251/50B01D2252/204B01D2252/504B01D2252/606B01D2258/0291Y02P20/129C01B32/50Y02C20/40Y02P20/151
Inventor FUJIMOTO, NORIKAZUHATTORI, KYOUHEIYAMAGUCHI, FUMIHIKO
Owner ASAHI KASEI KK
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