A Method of Pretreatment and Bromine Recovery of PCB Incineration Ash

Patent metadata

Field	Value
Publication number	US-2020262712-A1
Application number	US-201816348506-A
Country	US
Kind code	A1
Filing date	Dec 21, 2018
Priority date	Dec 30, 2017
Publication date	Aug 20, 2020
Grant date	—

Abstract

A method of pretreatment and bromine recovery of PCB Incineration ash is disclosed that relates to the field of comprehensive recovery of valuable metals by full wet method, especially relates to a method of valuable metals and bromine recovery, precious metals enrichment in pretreatment process of PCB Incineration ash. The major steps includes alkali leaching, Cu extraction back-extraction, neutralization-precipitation to separate, Bromine evaporative crystallization, regeneration, acid pickling, Zn evaporative crystallization, removal of Zn and Cu. Compared with the traditional comprehensive recovery process of ash, the invention can separate bromine from ash and recover valuable metals such as copper, zinc and lead with the maximum extent, at the same time, the enrichment of silver and other precious metals is beneficial to the subsequent recovery of precious metals. It has high added recovery value and no tailless discharge.

First claim

What is claimed is:

1 . A method of pretreatment and Bromine recovery of printed circuit board Incineration ash, comprising the steps of:
(1) alkali leaching, further comprising the steps of:
treating the printed circuit board Incineration ash with an alkali leaching solution for 1 to 2 hours, wherein the alkali leaching solution is made of a mixture of sodium hydroxide and ammonia, wherein the concentration of sodium hydroxide is 5˜20% by mass, and the concentration of ammonia is 5˜20% by mass, the solid-liquid ratio of ash to the leaching solution is 1:5˜1:10 Kg/L, the leaching temperature is 35˜55° C., meanwhile keep blowing air with agitation, wherein the blast air volume per cubic meter leaching solution is 0.01˜0.1 m 3 /min;
stopping blowing the air and continue agitating, adding 1˜3 g copper powder into every liter of the leaching solution;
carrying out the reaction for 10˜30 minutes; and
performing filtration to obtain a mixed alkali leaching slag and a mixed alkali leaching solution;
(2) Cu extraction back-extraction, further comprising the steps of:
extracting copper from the mixed alkali leaching solution from step (1) with Benzaldehyde, 2-hydroxy-5-nonul-,oxime, and
performing back-extraction with a sulfuric acid solution to obtain copper sulfate and raffinate;
(3) neutralization-precipitation, further comprising the steps of:
adding a sulfuric acid to the raffinate in step (2) for neutralization and precipitation, to obtain a precipitated slag and a precipitated solution;
(4) Bromine evaporative crystallization, further comprising the steps of:
performing bromine evaporative crystallization for the precipitated solution in step (3), to obtain Bromine salts and crystal mother liquor;
(5) regeneration, further comprising the steps of:
regenerating the crystal mother liquor in step (4) by adding lime, to obtain gypsum and post-regeneration solution, wherein the gypsum is put away to be treated concertedly,
(6) acid pickling, further comprising the steps of:
performing acid wash of the precipitated slag in step (3) with sulfuric acid to obtain lead sulfate and acid pickling solution;
(7) Zn evaporative crystallization, further comprising the steps of:
performing evaporative crystallization of the acid pickling solution in step (6), to obtain Zinc sulfate and crystallized solution, wherein the crystallized solution is returned to the acid pickling process as part of the acid washing solution; and
(8) removal of Zn and Cu, further comprising the steps of:
removing zinc and copper from the mixed alkali leaching slag in step (1), by contacting the mixed alkali leaching slag with a leaching solution of 100˜200 g/L sulfuric acid solution, the leaching temperature being 55˜75° C. and the leaching time being 1˜3 hours, and hydrogen peroxide is added during leaching, wherein the mass of hydrogen peroxide added to per liter of the leaching solution is 40˜80 g/L;
performing a filtration to obtain Copper/Zinc removal residual and copper/Zinc removal filtrate; and
separating Copper and Zinc from the copper/zinc removal filtrate to obtain Copper sulfate and Zinc sulfate; wherein the Copper/Zinc removal residual is used for the enrichment of precious metals and recovery of valuable metals

2 . The method of pretreatment and bromine recovery of printed circuit board Incineration ash according to claim 1 , wherein during the step (5) the post-regeneration solution is returned to the alkali leaching process of step (1) to form part of the alkali leaching solution.

3 . The method of pretreatment and bromine recovery of printed circuit board Incineration ash according to claim 1 , wherein in step (3) a terminal pH value of the precipitation is 6-7.

4 . The method of pretreatment and bromine recovery of printed circuit board Incineration ash according to claim 1 , wherein the pH in the step (5) regeneration is adjusted to 11-12.

5 . The method of pretreatment and bromine recovery of printed circuit board Incineration ash according to claim 1 , wherein in step (6) the precipitated slag is was acid washed with sulfuric acid until the washing solution had a pH of 1-3.

6 . The method of pretreatment and bromine recovery of printed circuit board Incineration ash according to claim 1 , wherein in step (7), the crystallized solution is returned to the acid pickling process as part of the acid washing solution.

Assignees

• Univ Beijing Technology

Inventors

• Wu Yufeng
• Pan Dean
• Li Bin
• Zuo Tieyong

Classifications

• C22B3/30

  Oximes · CPC title

• C22B7/02 Primary

  Working-up flue dust · CPC title

• C22B15/0065

  Leaching or slurrying (with organic compounds C22B3/16) · CPC title

• C22B7/04

  Working-up slag · CPC title

• C22B7/008

  by an alkaline or ammoniacal leaching · CPC title