Method of extracting and carbonating calcium from alkaline industrial waste or by-product materials

Patent metadata

Field	Value
Publication number	US-12157675-B2
Application number	US-201917299803-A
Country	US
Kind code	B2
Filing date	Dec 4, 2019
Priority date	Dec 4, 2018
Publication date	Dec 3, 2024
Grant date	Dec 3, 2024

Abstract

The present invention concerns a process for producing calcium carbonate from a calcium-containing alkaline slag material, the process containing the steps of
extracting the alkaline slag material in a series of extraction steps, including at least 2 extraction steps, using extraction solvent(s) containing salt in an aqueous solution, whereby a calcium-containing filtrate and a residual slag is formed in each extraction step, separating the residual slag from the filtrate after each extraction step, carrying each residual slag to the following extraction in the series of extractions, to be used as raw material in said following extraction, and discarding the residual slag separated from the last extraction, carrying each filtrate to the previous extraction in the series of extractions, to be used as extraction solvent in said previous extraction, and carrying the first filtrate, separated from the first extraction step, to a carbonating step, carbonating calcium as calcium carbonate from the first filtrate, the first filtrate also used as the carbonation solvent, and using a carbonation gas, whereby calcium carbonate precipitates, separating and recovering the calcium carbonate from the remaining carbonation solvent, and recycling the remaining carbonation solvent to the last extraction step in the series of extraction steps, to be used as extraction solvent.

First claim

The invention claimed is:

1. A process for producing calcium carbonate from a calcium-containing alkaline slag material, the process comprising:
extracting the alkaline slag material in a series of extraction steps, including at least 2 extractions, using extraction solvent(s) containing salt in an aqueous solution, whereby a calcium-containing filtrate and a residual slag is formed in each extraction step,
carrying out a step of extractive grinding simultaneously with a first extraction step of the series of extraction steps,
separating the residual slag from the calcium-containing filtrate after each extraction step,
carrying each residual slag to a following extraction in the series of extraction steps, to be used as raw material in said following extraction, and discarding the residual slag separated from the last extraction of the series of extraction steps,
carrying each calcium-containing filtrate to a previous extraction in the series of extraction steps, to be used as an extraction solvent in said previous extraction, and
carrying a first calcium-containing filtrate, separated from a first extraction step, to a carbonating step,
carbonating calcium as calcium carbonate from the first calcium-containing filtrate, the first calcium-containing filtrate also used as a carbonation solvent, and using a carbonation gas, whereby calcium carbonate precipitates,
separating and recovering the calcium carbonate from remaining carbonation solvent, and
recycling the remaining carbonation solvent to the last extraction step in the series of extraction steps, to be used as extraction solvent.

2. The process of claim 1 , wherein fresh extraction solvent is added to any of the extraction steps, wherein the remaining extraction steps are operated using the filtrates fed counter-currently from the subsequent extraction step, or from the carbonating step.

3. The process of claim 1 , wherein fresh extraction solvent is added to any of the series of extraction steps, the fresh extraction solvent being an aqueous solution comprising an aqueous solution of an ammonium salt.

4. The process of claim 1 , wherein fresh extraction solvent is added to any of the series of extraction steps, the fresh extraction solvent being an aqueous solution of ammonium chloride (NH 4 Cl).

5. The process of claim 3 , wherein the fresh extraction solvent has a pH value of 5-7.

6. The process of claim 1 , wherein the alkaline slag material is an iron- and steelmaking slag.

7. The process of claim 1 , wherein the carbonation gas is CO 2 or a CO 2 -containing gas.

8. The process of claim 1 , wherein the carbonation is carried out by bubbling the carbonation gas through the filtrate to be carbonated, or by spraying the filtrate into a flue gas scrubber.

9. The process of claim 1 , wherein a stream of CO 2 -lean gas, which did not react in the carbonation, is conducted away from the carbonation step, which stream of CO 2 -lean gas contains an amount of evaporated first extraction solvent, which solvent is condensed and combined with the remaining carbonation solvent to be recycled to the last extraction step.

10. The process of claim 1 , wherein the series of extraction steps are carried out at a temperature of 10-90° C.

11. The process of claim 1 , wherein a series of 2-30 extraction steps is used.

12. The process of claim 1 , further comprising, prior or concurrent step, prior to or simultaneously with to the first extraction step, wet milling the alkaline slag material.

13. The process of claim 12 , wherein the wet milling is done simultaneously with the first extraction step.

Assignees

• Aalto Univ Foundation Sr

Inventors

• Järvinen Mika
• Eloneva Sanni

Classifications

• C22B26/20

  Obtaining alkaline earth metals or magnesium · CPC title

• C22B7/04 Primary

  Working-up slag · CPC title

• C22B7/007

  by acid leaching · CPC title

• C22B7/008

  by an alkaline or ammoniacal leaching · CPC title

• C22B3/20

  Treatment or purification of solutions, e.g. obtained by leaching (C22B3/18 takes precedence) · CPC title