Method of treating fly ash of a recovery boiler

Patent metadata

Field	Value
Publication number	US-11725341-B2
Application number	US-201816609006-A
Country	US
Kind code	B2
Filing date	Apr 26, 2018
Priority date	Apr 28, 2017
Publication date	Aug 15, 2023
Grant date	Aug 15, 2023

Abstract

A method of treating fly ash containing sodium sulfate from a recovery boiler of a chemical pulp mill. This method includes at least the following steps: a) ash is dissolved in an aqueous solution and the pH of the solution is adjusted with alkali for precipitating impurities, b) the solution is filtered for removing the impurities containing precipitate, c) sodium sulfate is crystallized from the solution and the crystals are separated from the solution by filtering or by centrifugation, and d) the crystallized sodium sulfate is used as initial material for producing sodium and sulfur containing chemicals or as process chemical.

First claim

The invention claimed is:

1. A method of treating fly ash containing sodium sulfate from a recovery boiler of a chemical pulp mill, wherein the fly ash is removed from a chemical cycle of the chemical pulp mill for adjusting the chemical balance, said method comprising:
a) dissolving the fly ash in a first aqueous solution, and adjusting the pH of the first aqueous solution with alkali to precipitate impurities from the first aqueous solution with the fly ash,
b) filtering the first aqueous solution with the fly ash to remove the precipitated impurities,
c) crystallizing sodium sulfate in the filtered first aqueous solution with the fly ash to form sodium sulfate crystals,
d) separating the sodium sulfate crystals from the filtered first aqueous solution with the fly ash by filtering or centrifugation,
e) dissolving the sodium sulfate crystals in a second aqueous solution to form dissolved sodium sulfate crystals,
f) decreasing with acid the pH of the second aqueous solution with the dissolved sodium sulfate crystals to precipitate calcium from the second aqueous solution, and
g) after step f), using the dissolved sodium sulfate crystals as an initial material for producing sodium and sulfur containing chemicals and/or as a process chemical.

2. The method according to claim 1 , wherein the pH of the first aqueous solution with the fly ash is adjusted with the alkali to a level of over 11 in step a).

3. The method according to claim 1 , wherein the step of crystallizing the sodium sulfate crystals in the filtered first aqueous solution with the fly ash includes cooling crystallization and/or evaporation crystallization.

4. The method according to claim 1 , wherein the fly ash is dissolved in the step a) at a temperature in a range of 32° C. to 100° C.

5. The method according to claim 1 , wherein the method further comprises step removing the precipitated calcium from the second aqueous solution.

6. The method according to claim 1 , wherein the acid used in step e) is an acid salt produced in a chloride dioxide plant.

7. The method according to claim 1 , wherein the precipitated calcium is removed from the second aqueous solution with the dissolved sodium sulfate crystals using an ion-exchange column.

8. The method according to claim 1 , further comprising removing carbonate from the sodium sulfate crystals after step c).

9. The method according to claim 1 , wherein the dissolved sodium sulfate crystals are decahydrate of sodium sulfate or an anhydrous sodium sulfate.

10. The method according to claim 1 , wherein the dissolved sodium sulfate crystals are used as the initial material in an electrodialysis process or in an electrolysis process to produce sodium and sulfur chemicals.

11. The method according to claim 1 , wherein the dissolved sodium sulfate crystals are used outside the chemical pulp mill.

12. The method according to claim 1 , further comprising separating a chloride and potassium containing solution from the first filtered aqueous solution with the fly ash and the crystallized sodium sulfate crystals.

13. A method to treat fly ash comprising:
discharging fly ash from a recovery boiler in a chemical pulp mill;
dissolving the fly ash in a first aqueous solution;
precipitating impurities from the aqueous solution with the dissolved fly ash by adding alkaline to increase the pH level to at least eleven of the first aqueous solution with the dissolved fly ash;
filtering the first aqueous solution with the dissolved fly ash to remove the precipitated impurities and form a filtered first aqueous solution with the dissolved fly ash;
crystallizing sodium sulfate in the filtered first aqueous solution with the dissolved fly ash,
after the crystallization, separating crystallized sodium sulfate from the filtered first aqueous solution with the dissolved fly ash by filtering or centrifugation,
dissolving the crystallized sodium sulfate in a second aqueous solution to form dissolved crystallized sodium sulfate,
decreasing with acid the pH of the second aqueous solution with the dissolved crystallized sodium sulfate to precipitate calcium from the second aqueous solution, and
using the dissolved crystallized sodium sulfate to produce sodium and sulfur containing chemicals and/or as a process chemical.

14. The method according to claim 13 , wherein the first aqueous solution in the step of dissolving of the fly ash is at a temperature in a range of 32° C. to 100° C.

15. The method according to claim 13 , further comprising precipitating calcium from the filtered first aqueous solution with the dissolved fly ash.

16. The method according to claim 13 , wherein the calcium is precipitated from the dissolved crystallized sodium sulfate in the second aqueous solution in an ion-exchange column.

17. The method according to claim 16 , further comprising using the dissolved crystallized sodium sulfate in an electrodialysis process or in an electrolysis process to produce the sodium and the sulfur chemicals.

Assignees

• Andritz Oy

Inventors

• Salmenoja Keijo
• Metsämuuronen Niko
• Joutsimo Marjukka
• Reilama Ismo

Classifications

• D21C11/0007

  Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for (volatile compounds obtained by decomposition of spent liquors in order to regenerate them D21C11/125; compounds obtained by fractionating the liquors in order to regenerate them D21C11/0042) · CPC title

• B01D9/00

  Crystallisation (crystallisation directly from the vapour phase B01D7/02; making single crystals C30B {; crystallisation as part of the Bayer process also classified in C01F7/14}) · CPC title

• C01D5/00 Primary

  Sulfates or sulfites of sodium, potassium or alkali metals in general {(sulfites in general C01B17/62)} · CPC title

• D21C11/066 Primary

  Separation of solid compounds from these gases; further treatment of recovered products · CPC title

• B01D9/005

  Selection of auxiliary, e.g. for control of crystallisation nuclei, of crystal growth, of adherence to walls; Arrangements for introduction thereof · CPC title