发明名称 |
Hydrometallurgical plant of nickel laterite ore and operation method thereof |
摘要 |
A hydrometallurgical plant for nickel laterite ore extraction having a plurality of treatment facility lines wherein the plant is capable of minimizing a decrease in throughput when line failure occurs and efficiently restoring normal operation status Each line of the treatment facility includes a pretreatment step, a leaching step, a solid-liquid separation step, a neutralization step, a zinc removal step, a sulfurization step and a detoxification step. The lines are coupled by pipelines, each having a valve, installed after the solid-liquid separation step for sending a liquid from the solid-liquid separation step to the neutralization step in each line and/or after the sulfurization step for sending a liquid from the sulfurization step to the detoxification step in each line. |
申请公布号 |
US8911531(B2) |
申请公布日期 |
2014.12.16 |
申请号 |
US201013394202 |
申请日期 |
2010.10.01 |
申请人 |
Sumitomo Metal Mining Co., Ltd. |
发明人 |
Nakai Osamu;Kitazaki Toru;Heguri Shinichi;Ozaki Yoshitomo;Shibayama Keisuke |
分类号 |
C22B3/04;C22B3/00;C22B3/02 |
主分类号 |
C22B3/04 |
代理机构 |
Westerman, Hatori, Daniels & Adrian, LLP |
代理人 |
Westerman, Hatori, Daniels & Adrian, LLP |
主权项 |
1. A hydrometallurgical plant of a nickel laterite ore comprising;
two or more lines of a series of treatment facilities, wherein the treatment facilities consist of a pretreatment step, a leaching step, a solid-liquid separation step, a neutralization step, a zinc removal step, a sulfurization step and a detoxification step, and wherein the lines are coupled by installing a first coupling pipeline having a first valve positioned after the solid-liquid separation step in the lines and a second coupling pipeline having a second valve positioned after the sulfurization step in the lines; wherein the first coupling pipeline transfers a liquid from the solid-liquid separation step to the neutralization step between each line and the second coupling pipeline transfers a liquid from the sulfurization step to the detoxification step between each line wherein the transfer from the solid-liquid separation step to the neutralization step consists only of the liquid from the solid-liquid separation step, and wherein the transfer from the sulfurization step to the detoxification step consists only of the liquid from the sulfurization step. |
地址 |
Tokyo JP |