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首页> 外文期刊>Separation and Purification Technology >Leaching and concentration of P and K from P-K associated ore by using a sequential leaching process with leachate recycling
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Leaching and concentration of P and K from P-K associated ore by using a sequential leaching process with leachate recycling

机译:通过使用序列浸出过程与渗滤液再循环的序列浸出方法,P-K相关矿石的浸出和浓度p和k

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摘要

The concentrations of P and K in leaching solution are relatively low and the consumption of acid is relatively large, which are the existing problems in the leaching of P and K from P-K associated ore by using the low-temperature acid leaching process. In this work, a sequential leaching process with leachate recycling was developed, in which P and K were sequentially leached out from P-K associated ore and the obtained P- and K-containing leachates were recycled into the next leaching process. In this sequential process with leachate recycled two times the concentrations of K and P2O5 in leachate were increased from 20.18 and 15.79 g/L to 53.26 and 45.97 g/L, respectively. In comparison, in the simultaneous leaching process with leachate recycling both the leaching efficiencies of K and P and the concentrations of K and P2O5 were significantly lower than those in the sequential leaching process, which can be mainly attributed to the fact that Ca in the ore, which could react with PO43- to generate Ca-containing sediments, was precipitated first in the sequential leaching process. The sequential leaching process with leachate recycling will provide an efficient method for leaching and concentrating P and K from P-K associated ore.
机译:浸出溶液中的P和K的浓度相对较低,酸的消耗相对较大,这是通过使用低温酸浸出工艺从P-K相关矿石浸出P和K中的存在问题。在这项工作中,开发了一种序列浸出过程,其中序列浸出过程从P-K相关矿石中依次浸出P和K,并将所得的P-和K含钾渗滤液再循环到下一个浸出过程中。在该序列过程中,渗滤液再循环两倍,渗滤液中K和P 2 O 5的浓度分别从20.18和15.79g / L至53.26和45.97g / L增加。相比之下,在具有渗滤液再循环的同时浸出过程中,K和P的浸出效率以及K和P2O5的浓度显着低于顺序浸出过程中的浓度,这可能主要归因于矿石中的CA可以与PO43-产生含Ca沉积物的,首先在连续的浸出过程中沉淀。具有渗滤液再循环的顺序浸出过程将提供一种有效的浸出和浓缩p和k的方法,来自p-k相关矿石。

著录项

  • 来源
  • 作者单位

    Wuhan Inst Technol Sch Chem Engn &

    Pharm Key Lab Green Chem Proc Minist Educ Wuhan 430205 Hubei Peoples R China;

    Wuhan Inst Technol Sch Chem Engn &

    Pharm Key Lab Green Chem Proc Minist Educ Wuhan 430205 Hubei Peoples R China;

    Wuhan Inst Technol Sch Chem Engn &

    Pharm Key Lab Green Chem Proc Minist Educ Wuhan 430205 Hubei Peoples R China;

    Wuhan Inst Technol Sch Chem Engn &

    Pharm Key Lab Novel Reactor &

    Green Chem Technol Hubei Wuhan 430205 Hubei Peoples R China;

    Wuhan Inst Technol Sch Chem Engn &

    Pharm Key Lab Novel Reactor &

    Green Chem Technol Hubei Wuhan 430205 Hubei Peoples R China;

    Wuhan Inst Technol Sch Chem Engn &

    Pharm Key Lab Novel Reactor &

    Green Chem Technol Hubei Wuhan 430205 Hubei Peoples R China;

    Wuhan Inst Technol Sch Chem Engn &

    Pharm Key Lab Novel Reactor &

    Green Chem Technol Hubei Wuhan 430205 Hubei Peoples R China;

    Wuhan Inst Technol Sch Chem Engn &

    Pharm Key Lab Novel Reactor &

    Green Chem Technol Hubei Wuhan 430205 Hubei Peoples R China;

    Wuhan Inst Technol Sch Chem Engn &

    Pharm Key Lab Novel Reactor &

    Green Chem Technol Hubei Wuhan 430205 Hubei Peoples R China;

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 分离过程;气化工艺;
  • 关键词

    P-K associated ore; Potash feldspar; Sequential leaching; Simultaneous leaching; Leachate recycling;

    机译:P-K相关矿石;Potash Feldspar;连续浸出;同时浸出;渗滤液再循环;

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