BIPOLAR ELECTRODIALYZER AND PURIFICATION METHOD FOR AMINE FLUID USING SAME

• US 20150290576A1
• Filed: 11/15/2013
• Published: 10/15/2015
• Est. Priority Date: 11/16/2012
• Status: Abandoned Application

• Current Assignee: Asahi Kasei Kabushiki Kaisha (Asahi Kasei Corporation)
• Original Assignee: Asahi Kasei Kabushiki Kaisha (Asahi Kasei Corporation)
• Inventors: Fujimoto, Norikazu, Kiguchi, Akira
• Application Number:
  US14/442,900
• Publication Number:
  US 20150290576A1
• Time in Patent Office: Days
• US Class Current: 1/1
• CPC Class Codes: B01D 2311/2626 Absorption or adsorption
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: B01D 53/1475 Removing carbon dioxide
• CPC Class Codes: B01D 53/965 including an electrochemical process step
• CPC Class Codes: B01D 61/445 with bipolar membranes; Water splitting
• CPC Class Codes: B01D 61/54 Controlling or regulating
• CPC Class Codes: C01B 32/50 Carbon dioxide
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02P 20/151 Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Abstract

Provided is an electrodialyzer for regenerating amines, comprising a negative electrode, a positive electrode, a bipolar film, and an anion exchange film. The electrodialyzer includes a chamber having an amine purification function, a chamber having an amine recovery function, and a chamber having an acid recovery function, between the facing negative electrode and positive electrode and in order in the direction from the negative electrode towards the positive electrode. The chamber having the amine purification function is surrounded by the bipolar film arranged on the negative electrode side and the anion exchange film arranged at a position facing the bipolar film. The chamber having the amine recovery function is surrounded by a set of facing anion exchange films, and the chamber having an acid recovery function is surrounded by the anion exchange film arranged on the negative electrode side, and the positive electrode or bipolar film arranged at a position facing the anion exchange film.

Claims

1. An electrodialyzer for regenerating an amine, comprising:

a negative electrode;

a positive electrode opposing the negative electrode;

at least one bipolar membrane; and

anion exchange membranes,

wherein one of the at least one bipolar membrane on the negative-electrode side and one of the anion exchange membranes in a position so as to face each other, form a compartment having an amine purification function,

a pair of the anion exchange membranes in which each membrane opposes the other, form a compartment having an amine recovery function,

another of the anion exchange membranes on the negative-electrode side and the positive electrode or another of the at least one bipolar membrane in a position so as to face each other, form a compartment having an acid recovery function, and

between the negative electrode and the positive electrode, the compartment having an amine purification function, the compartment having an amine recovery function and the compartment having an acid recovery function are arranged in a direction from the negative electrode to the positive electrode.

2. The electrodialyzer according to claim 1, wherein the compartment having an acid recovery function is formed by another of the anion exchange membranes on the negative-electrode side and another of the at least one bipolar membrane in a position so as to face each other.

3. The electrodialyzer according to claim 1 or 2, wherein the electrodialyzer has a three-compartment structure in which an amine purification compartment, an amine recovery compartment and an acid recovery compartment are arranged in this order between the negative electrode and the positive electrode.

4. The electrodialyzer according to claim 1, wherein the amine is a primary amine and/or a secondary amine, and the electrodialyzer further includes a control mechanism for controlling the pH in the compartment having an amine recovery function within the range from 0 to 7.

5. A method for purifying an amine solution, comprising:

a step of providing the electrodialyzer according to claim 1;

a step of introducing the amine solution into the compartment having an amine purification function;

a step of subjecting the amine solution to electrodialysis in the electrodialyzer;

a step of recovering an amine which has permeated at least one of the anion exchange membranes, from the compartment having an amine recovery function; and

a step of removing an acid recovery solution from the compartment having an acid recovery function.

6. The method according to claim 5, wherein the amine solution contains a component having a vapor pressure of 0.1 atm or less at 140°

C.

7. The method according to claim 5 or 6, wherein the amine solution further contains boric acid and/or amino acid.

8. A carbon dioxide separation/recovery apparatus comprising an absorption column, a regeneration column, and the electrodialyzer according to claim 1, wherein

the absorption column has a means for contacting an amine solution with a gas containing carbon dioxide to obtain a carbon dioxide-containing amine solution,

the regeneration column has a means for heating the carbon dioxide-containing amine solution to separate carbon dioxide, and

the electrodialyzer has a means for maintaining a concentration of an acidic component in the amine solution at less than 3.0 mass %.

9. The apparatus according to claim 8, further comprising:

a heat exchanger for cooling the amine solution which has been regenerated in the regeneration column; and

a control mechanism for adjusting the concentration of the acidic component in the amine solution removed from the electrodialyzer to less than 50% of the concentration of the acidic component in the amine solution before being introduced into the electrodialyzer.