Method for recovering alkali and aluminum in course of treatment of bayer red mud by using calcification-carbonation method

Patent metadata

Field	Value
Publication number	US-9963353-B2
Application number	US-201415303408-A
Country	US
Kind code	B2
Filing date	Jul 22, 2014
Priority date	Apr 30, 2014
Publication date	May 8, 2018
Grant date	May 8, 2018

Abstract

A method for recovering alkali and aluminum during treatment of Bayer red mud using a calcification-carbonation method, including steps of mixing the Bayer red mud with calcium aluminate or with calcium aluminate and lime, performing calcification dealkalization conversion in a high-concentration alkaline liquor, and carbonizing the calcified residues produced during dealkalization to obtain carbonized residues; and then performing low-temperature aluminum dissolution, aluminum precipitation and the like to obtain calcium aluminate products, which is returned to the calcification dealkalization conversion of the red mud for recycling. Part of an alkali-containing and aluminum-containing liquid phase after calcification dealkalization conversion can be used as supplementary alkali in the Bayer production course for recycling. The method is energy-saving and environmentally-friendly, and allows recovering alkali and aluminum from the red mud and harmless treatment of the Bayer red mud.

First claim

What is claimed is:

1. A method for recovering alkali and aluminum in the course of treatment of Bayer red mud by using a calcification-carbonation method, the method comprising the following steps of
Step (1):
mixing the Bayer red mud with calcium aluminate or with calcium aluminate and lime, and performing a calcification dealkalization conversion reaction in mother liquor of a high-concentration caustic alkaline solution, wherein the reaction temperature is 80-180° C. and the reaction time is 10-60 min, to form a solid phase of calcified residues of which the main component is hydrated garnet, and a liquid phase of the high-concentration caustic alkaline solution;
Step (2):
mixing clear water with the calcified residues at a liquid-solid amount of 3-15 ml clear water per 1 g calcified residues in a sealed container, and filling the sealed container with CO 2 , so that the partial pressure of CO 2 gas in the sealed container reaches 0.8-1.8 MPa; then performing a carbonization conversion reaction at 80-160° C. for 10-240 min to obtain a mineral pulp; and performing liquid-solid separation on the mineral pulp to obtain a solid phase of carbonization converted residues of which the main components are calcium silicate, calcium carbonate and aluminum hydroxide, and a liquid phase of water which is then recycled;
Step (3): under a reaction temperature of 40-100° C. and a reaction time of 20-120 min, enabling the carbonization converted residues and a low-temperature aluminum dissolution mother liquor containing sodium hydroxide of which the concentration is 50-150 g/L to be subjected to an aluminum dissolution reaction, wherein the liquid to solid amount is 4-15 mL of the low-temperature aluminum dissolution mother liquor per 1 g of the carbonization converted residues, so as to obtain a mineral pulp; performing liquid-solid separation on the mineral pulp to obtain a liquid phase of a sodium aluminate solution, and a solid phase of a novel-structure red mud of which the main components are calcium carbonate and calcium silicate;
performing step (2) and step (3) 1 to 5 times; and
washing the novel-structure red mud with water, and then discharging the washed red mud, wherein the washing liquid resulting from washing is returned to step (1) to be used for replenishing the water loss due to replenishing alkaline liquor from the high-concentration caustic alkaline solution for a Bayer method or step (3); and
Step (4):
enabling the sodium aluminate solution produced in step (3) to react with calcium-containing minerals so as to obtain calcium aluminate precipitates and a sodium hydroxide solution;
enabling the calcium aluminate precipitates from the reaction to be returned to step (1) to be recycled as a calcium source for the calcification dealkalization conversion reaction; and

enabling the sodium hydroxide solution to be returned to the step (3) to be recycled as mother liquor for low-temperature aluminum dissolution,
wherein, part of alkaline liquor is taken from the high-concentration caustic alkaline solution obtained in step (1) to replenish alkali for the Bayer method or step (3), and the alkaline liquor without being taken is recycled as the mother liquor of step (1).

2. The method according to claim 1 , wherein, the mass ratio of the calcium oxide in the calcium aluminate or the lime and the calcium aluminate to the red mud in step (1) is (0.2-1.0) to 1; and the liquid to solid amount is 3-10 mL of the mother liquor of the high-concentration caustic alkaline solution per 1 g of the red mud with the calcium aluminate or with a mixture of the lime and the calcium aluminate.

3. The method according to claim 1 , wherein, the mother liquor of the high-concentration caustic alkaline solution in step (1) is a sodium hydroxide solution containing sodium oxide of which the concentration is 100-300 g/L, or a sodium aluminate solution containing sodium oxide of which the concentration is 100-300 g/L.

4. The method according to claim 1 , wherein, V replenishing /V total , which is a ratio of the volume (V replenishing ) of the high-concentration caustic alkaline solution which is taken out to the volume (V total ) of the high-concentration caustic alkaline solution obtained after the calcification dealkalization conversion reaction, is associated with the concentrations of the caustic alkaline solutions before and after the calcification dealkalization conversion reaction, and the specific calculation relationship is as follows:

V
replenishing

V
total

=

m
after

-

m
before

m
before

wherein, V replenishing is the volume of the high-concentration caustic alkaline solution which is taken out, V total is the total volume of the high-concentration caustic alkaline solution after the calcification dealkalization conversion reaction, m after is the concentration of the caustic alkaline solution in the liquid phase after the calcification dealkalization conversion reaction, and m before is the concentration of the caustic alkaline solution in the liquid phase before the calcification dealkalization conversion reaction.

5. The method according to claim 1 , wherein, the calcium-containing minerals in step (4) are raw materials containing calcium oxides including lime, calcium aluminate and carbide residues; and the mass ratio of the calcium oxide in the calcium-containing mineral to the aluminium oxide in the sodium aluminate solution is (1.3-2.5) to 1.

6. The method according to claim 1 , wherein, the calcium-containing minerals and the sodium aluminate solution in step (4) react under a condition that the reaction temperature is 20-90° C. and the reaction time is 1-60 min.

Assignees

• Univ Northeastern

Inventors

• Zhang Tingan
• Lv Guozhi
• Liu Yan
• Zhang Zimu
• Zhu Xiaofeng
• Dou Zhihe

Classifications

• C01D1/04

  Hydroxides · CPC title

• C01F7/47 Primary

  of aluminates, e.g. removal of compounds of Si, Fe, Ga or of organic compounds from Bayer process liquors · CPC title

• C01F7/20

  Preparation of aluminium oxide or hydroxide from aluminous ores using acids or salts · CPC title

• B09B3/00

  Destroying solid waste or transforming solid waste into something useful or harmless · CPC title

• C01F7/16

  Preparation of alkaline-earth metal aluminates or magnesium aluminates; Aluminium oxide or hydroxide therefrom (C01F7/028 takes precedence) · CPC title