Apparatus and method for absorbing and mineralizing carbon dioxide

Patent metadata

Field	Value
Publication number	US-2017182458-A1
Application number	US-201615276218-A
Country	US
Kind code	A1
Filing date	Sep 26, 2016
Priority date	Dec 29, 2015
Publication date	Jun 29, 2017
Grant date	—

Abstract

The present invention relates to an apparatus for absorbing and mineralizing carbon dioxide comprising a reactor and a three-phase separator, in which said reactor comprises a tower body and a draft tube disposed inside the tower body, a liquid inlet pipe and a gas intake pipe being disposed on the tower body, the outlet ends of the liquid inlet pipe and the gas intake pipe both being located inside the draft tube; and the three-phase separator is disposed at the upper end of the reactor, and a method therefor. The arrangement of draft tube inside the reactor of the present invention, enhances gas-liquid-solid mixing state because of the flow with airlift loop flow inside the reactor, accelerates the dissolution rate of solid alkali solute and thus may increase absorption reaction rate and absorptivity; the integration of three-phase separator in the reaction apparatus may isolate carbonate by settling while reacting, reduce solid content of the solution, while reducing the circulation of water between absorption and separation units, improve process performance, reduce process energy consumption; carbonate particles generated can be controlled better, thus a higher settling efficiency can be obtained.

First claim

1 . An apparatus for absorbing and mineralizing carbon dioxide is characterized in comprising a reactor and a three phase separator, said reactor is arranged vertically and comprises a tower body and a draft tube, said draft tube being coaxially disposed inside said tower body, a liquid inlet pipe and a gas intake pipe being disposed on said tower body, the outlet ends of said liquid inlet pipe and said gas intake pipe both passing through said tower body and being located inside said draft tube; said three-phase separator includes a housing, a riser tube and a downcomer, the lower end of said housing being connected to the upper end of said reactor, the lower end of said riser tube communicating with the reactor, with the upper end extending inside said downcomer, an opening being disposed at lower end of said downcomer, a down flow channel being formed between said riser tube and said downcomer; a setting zone being formed between said housing and said downcomer, said down flow channel communicating with the setting zone.

2 . The apparatus for absorbing and mineralizing carbon dioxide according to claim 1 is characterized in that said draft tube is provided with openings at the upper and the lower ends, the outlets of said liquid inlet pipe and said gas intake pipe being located inside the opening of the lower end of said draft tube, and the outlet of said liquid inlet pipe being located above the outlet of said gas intake pipe.

3 . The apparatus for absorbing and mineralizing carbon dioxide according to claim 2 is characterized in that a gas distributor is provided at the outlet of said liquid inlet pipe.

4 . The apparatus for absorbing and mineralizing carbon dioxide according to claim 1 is characterized in that said tower body and said draft tube are both cylindrical configuration, with a height ratio of 0.5:1 to 0.8:1 and a diameter ratio of 0.6:1 to 0.75:1 thereof.

5 . The apparatus for absorbing and mineralizing carbon dioxide according to claim 1 is characterized in that sieve pores are provided on said draft tube, the area of said sieve pores is less than 0.4 times of the cross-sectional area of said draft tube.

6 . The apparatus for absorbing and mineralizing carbon dioxide according to claim 1 is characterized in that said three phase separator comprises a first drain pipe, a gas outlet and a second drain pipe, said first drain pipe being used for discharging supernatant liquid in the three-phase separator, said gas outlet being used for discharging the treated gas, and said second drain pipe being used for discharging bottom liquid in said three-phase separator.

7 . The apparatus for absorbing and mineralizing carbon dioxide according to claim 6 is characterized in that said first drain pipe and second drain pipe are located on upper portion and bottom portion of said setting zone, respectively, and said gas outlet is located at the upper end of said housing.

8 . The apparatus for absorbing and mineralizing carbon dioxide according to claim 1 is characterized in that the ratio of the cross-sectional area of said setting zone along radial direction of said housing to that along radial direction of said tower body is 1.5:1 to 4:1.

9 . The apparatus for absorbing and mineralizing carbon dioxide according to claim 8 is characterized in further comprising an overflow weir, said overflow weir is disposed inside said housing along the circumferential direction, and fixed on lower side of said first drain pipe.

10 . The apparatus for absorbing and mineralizing carbon dioxide according to claim 9 is characterized in that an overflow groove with an upward opening is formed by said overflow weir and inner wall of the housing, the height difference between the opening edge of said overflow groove and the upper end of the riser tube is 0.3 to 1 times of the diameter of said riser tube.

11 . A method for absorbing and mineralizing carbon dioxide is characterized in that carbon dioxide is absorbed and mineralized with alkali liquor by using the apparatus for absorbing and mineralizing carbon dioxide in any of claims 1 to 10 ; the volume faction of carbon dioxide in the gas to be treated is 0.05% to 20%, the volume of carbon dioxide intake per minute is 0.02 to 0.2 times of the volume of said reactor; the superficial gas velocity calculated by entirety of volume is 0.5˜8 cm/s.

12 . The method for absorbing and mineralizing carbon dioxide according to claim 11 is characterized in that said alkali liquor reacts with carbon dioxide to generate a solution or suspension of insoluble carbonate matter.

13 . The method for absorbing and mineralizing carbon dioxide according to claim 12 is characterized in that said alkali liquor is a suspension of calcium and/or magnesium hydroxide wherein the content of hydroxide is 1˜1500 times of its saturation solubility; the ratio of the molar flow rate of the hydroxide ion to the molar flow rate of the carbon dioxide is 0.5:1 to 4:1.

14 . The method for absorbing and mineralizing carbon dioxide according to claim 12 is characterized in that said alkali liquor is a suspension of mixture of calcium and/or magnesium hydroxide and hydrochloride or sulfate of calcium and/or magnesium, in which the content of the hydroxide is 1 to 1,500 times of its saturation solubility thereof, the molar ratio of salts to hydroxides is 0:1 to 4:1; the ratio of molar flow rate of hydroxide ion to the molar flow rate of carbon dioxide is 0.5:1 to 4:1.

15 . The method for absorbing and mineralizing carbon dioxide according to claim 12 is characterized in that said alkali liquor is a solution of weak acid salt of calcium and/or magnesium, the pKa value of the acid corresponding to weak acid radical contained is greater than the pKa value of carbonic acid; and the ratio of the molar flow rate of the weak acid radical to the molar flow rate of carbon dioxide is 2:1 to 10:1.

16 . The method for absorbing and mineralizing carbon dioxide according to claim 12 is characterized in that said alkali liquor is aqueous ammonia dissolved with hydrochloride or sulfate of calcium and/or magnesium, the mass fraction of ammonia is 2 to 20%, the molar ratio of salt to ammonia is 0.2:1 to 2:1; the ratio of molar flow rate of ammonia to molar flow rate of carbon dioxide is 0.5:1 to 4:1.

17 . The method for absorbing and mineralizing carbon dioxide according to claim 12 is characterized in that said alkali liquor is ethanolamine, diethanolamine, or a mixture of methyldiethanolamine with aqueous solution of sulphate or hydrochloride of calcium and/or magnesium, the mass fraction of ethanolamine, diethanolamine, or methyldiethanolamine is 5 to 30%, the molar ratio of the salts to said alcohol amine is 0.2:1 to 2:1; and the ratio of molar flow rate of amine group to molar flow rate of carbon dioxide is 0.5:1 to 4:1.

Assignees

• Yuanchu Tech (Beijing) Co Ltd
• Univ Tsinghua

Inventors

• Jiang Guoqiang
• Zhang Jiantao
• Yu Changjun
• Ding haichuan

Classifications

• B01D53/62 Primary

  Carbon oxides · CPC title

• B01D2251/402

  of magnesium · CPC title

• B01D53/18

  Absorbing units; Liquid distributors therefor (B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32) · CPC title

• B01D2251/604

  Hydroxides · CPC title

• B01D2251/404

  of calcium · CPC title