4SCN溶液解吸Re,實(shí)現(xiàn)Re/Sb/Bi的分步解吸并獲得錸富集液。結(jié)果表明:酸洗液電位對(duì)Re、Sb、Bi吸附率沒(méi)有明顯影響,適宜的酸洗液H2SO4濃度約43 g.L-1,Re、Sb、Bi吸附率分別為100%、6.55%和89.05%;D296樹(shù)脂吸附Re的穿透容量和飽和容量分別為1.308 g.L-1和1.773 g.L-1,且樹(shù)脂利用率為73.77%;先采用12.5%氨水解吸Sb,16% NaOH+140 g.L-1酒石酸混合溶液解吸Bi,通過(guò)添加酒石酸可有效抑制Bi水解,再采用10% NH4SCN溶液解吸Re,得到錸富集液,其Cu、As、Sb、Bi均降至1mg.L-1以下,且使酸洗液中Re富集了4倍。"/>

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從銅冶煉煙氣酸洗液中分離富集錸
作者:
作者單位:

1.西安建筑科技大學(xué) 冶金工程學(xué)院;2.西北有色金屬研究院

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中圖分類號(hào):

TF841.8

基金項(xiàng)目:

國(guó)家重點(diǎn)研發(fā)計(jì)劃項(xiàng)目(2018YFC1901704)


Separation and enrichment of rhenium from acid washing solutionof copper smelting flue gas
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Affiliation:

1.School of Metallurgical Engineering,Xi'an University of Architecture and Technology,Xi’an;2.Northwest Institute for Nonferrous Metal Research,Xi’an

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    摘要:

    銅冶煉煙氣酸洗液經(jīng)D296陰離子交換樹(shù)脂吸附后,再依次采用氨水解吸Sb,NaOH和酒石酸混合溶液解吸Bi,NH4SCN溶液解吸Re,實(shí)現(xiàn)Re/Sb/Bi的分步解吸并獲得錸富集液。結(jié)果表明:酸洗液電位對(duì)Re、Sb、Bi吸附率沒(méi)有明顯影響,適宜的酸洗液H2SO4濃度約43 g.L-1,Re、Sb、Bi吸附率分別為100%、6.55%和89.05%;D296樹(shù)脂吸附Re的穿透容量和飽和容量分別為1.308 g.L-1和1.773 g.L-1,且樹(shù)脂利用率為73.77%;先采用12.5%氨水解吸Sb,16% NaOH+140 g.L-1酒石酸混合溶液解吸Bi,通過(guò)添加酒石酸可有效抑制Bi水解,再采用10% NH4SCN溶液解吸Re,得到錸富集液,其Cu、As、Sb、Bi均降至1mg.L-1以下,且使酸洗液中Re富集了4倍。

    Abstract:

    The acid washing solution of copper smelting flue gas was adsorbed by D296 anion exchange resin, and then Sb was desorbed by ammonia, Bi was desorbed by NaOH and tartaric acid mixed solution, and Re was desorbed by NH4SCN solution. The step-by-step desorption of Re/Sb/Bi was realized and rhenium enrichment solution was obtained. The results show that the potential of acid washing solution has no significant effect on the adsorption rates of Re, Sb and Bi. The appropriate concentration of H2SO4 in acid washing solution is about 43 g.L-1, and the adsorption rates of Re, Sb and Bi are 100%, 6.55% and 89.05%, respectively. The breakthrough capacity and saturation capacity of D296 resin for adsorption of Re are 1.308 g.L-1 and 1.773 g.L-1, respectively, and the utilization rate of resin is 73.77%. Firstly, 12.5% ammonia is used to desorb sb, and 16% NaOH + 140 g.L-1 tartaric acid mixed solution is used to desorb Bi. The hydrolysis of Bi can be effectively inhibited by adding tartaric acid, and then 10% NH4SCN solution is used to desorb Re to obtain rhenium enrichment solution. The concentration of Cu, As, Sb and Bi in rhenium enrichment solution decrease to less than 1 mg.L-1. Re concentration in acid washing solution is enriched four times.

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陳昆昆,李林波,操齊高,張卜升.從銅冶煉煙氣酸洗液中分離富集錸[J].稀有金屬材料與工程,2023,52(1):345~350.[Chen Kunkun, Li Linbo, Cao Qigao, Zhang Bosheng. Separation and enrichment of rhenium from acid washing solutionof copper smelting flue gas[J]. Rare Metal Materials and Engineering,2023,52(1):345~350.]
DOI:10.12442/j. issn.1002-185X.20211139

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  • 收稿日期:2021-12-21
  • 最后修改日期:2022-01-22
  • 錄用日期:2022-02-09
  • 在線發(fā)布日期: 2023-02-13
  • 出版日期: 2023-02-08