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A method for preparing iron phosphate and iron pyrophosphate by using leaching tailings as iron source

A technology of iron pyrophosphate and iron phosphate, which is applied in the field of comprehensive utilization of industrial wastewater, can solve the problems of no use value, difficult treatment, difficult precipitation, etc., and achieve the effect of resource utilization, easy precipitation and recovery, and broad market prospects

Inactive Publication Date: 2016-08-31
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the colloidal nature of the former, it is difficult to precipitate, which causes great difficulties for subsequent treatment, and the mixture of ferric hydroxide and calcium sulfate is basically useless and can only be stored in tailings ponds, which not only occupies land, but also still exists in the environment. Hidden danger
[0004] On the other hand, after the copper, lead, zinc and other industrial elements in the leaching tailings are extracted, the purity and concentration of iron ions are relatively high. The existing treatment methods for this type of wastewater do not consider the recycling of iron, resulting in waste of resources

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] 1) One thousand liters of leaching tailings from a mine, containing 9.8 g / L of iron, pour a 5% trisodium phosphate solution into the leaching tailings pool, stir and check the pH until the pH reaches 3.0 and precipitates form ;

[0028] 2) Spray 5 kg of non-ionic polyacrylamide (PAM) solution with a concentration of 0.1% evenly into the tail liquid pool and stir;

[0029] 3) Stand still for 8 hours to precipitate the suspension, dehydrate the precipitate by pressure filtration, rinse with cold water, and dry the solid phase at 90°C to obtain ferric phosphate.

Embodiment 2

[0031] 1) One thousand liters of ore leaching tailings from a mine, containing 15.6 g / L of iron, pour 10% disodium hydrogen phosphate solution into the leaching tailings pool, stir and check the pH until the pH reaches 3.5 and there is precipitation form;

[0032] 2) Spray 50 kg of non-ionic polyacrylamide (PAM) solution with a concentration of 0.01% evenly into the tail liquid pool and stir;

[0033] 3) Stand still for 4 hours to precipitate the suspension, dehydrate the precipitate by pressure filtration, rinse with cold water, and dry the solid phase at 80°C to obtain ferric phosphate.

Embodiment 3

[0035] 1) One thousand liters of leaching tailings from a mine, containing 21 g / L of iron, pour 8% sodium dihydrogen phosphate solution into the leaching tailings pool, stir and check the pH until the pH reaches 4.5 and there is precipitation form;

[0036] 2) Spray 20 kg of non-ionic polyacrylamide (PAM) solution with a concentration of 0.05% evenly into the tail liquid pool and stir;

[0037] 3) Stand still for 6 hours to precipitate the suspension, dehydrate the precipitate by pressure filtration, rinse with cold water, and dry the solid phase at 90°C to obtain ferric phosphate.

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PUM

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Abstract

The invention discloses a method for preparing ferric phosphate and ferric pyrophosphate by using an ore leaching tail liquid as an iron source. The method comprises the following steps: 1) while stirring, spraying a 5-10 wt% phosphate or pyrophosphate solution into the ore leaching tail liquid until the pH value is equal to 3.5-4.5 and a precipitate is formed; 2) standing for 0.5-2 hours, and spraying a 0.1-0.3% organic flocculant solution into the suspension, wherein the flocculant solution accounts for 0.5-5 wt% of the ore leaching tail liquid; and 3) standing for 4-12 hours to precipitate the suspension, dewatering the precipitate by vacuum filtration or pressure filtration, eluting with cold water, and baking the solid phase at 80-90 DEG C to obtain the ferric phosphate or ferric pyrophosphate. On the premise of implementing harmless treatment on the ore leaching tail liquid, the method recovers the dissolved-state iron in the ore leaching tail liquid, and the obtained ferric phosphate or ferric pyrophosphate is a raw material for preparing lithium ion batteries.

Description

technical field [0001] The invention relates to a comprehensive utilization technology of industrial waste water, in particular to a method for preparing iron phosphate and iron pyrophosphate by using ore leaching tailing liquid as an iron source. Background technique [0002] Heap leaching of low-grade sulfide ores is often used to extract useful elements in the ore. When the useful elements are extracted, the resulting leaching tailings are bulky, strongly acidic, and contain a high concentration of ferric sulfate And sulfuric acid, improper disposal will cause great harm to the environment. [0003] At present, lime milk neutralization method is mostly used to treat this kind of wastewater. The neutralization process will produce a large amount of suspended solids, mainly iron hydroxide and calcium sulfate. Because the former has a colloidal nature, it is difficult to precipitate, which causes great difficulties for subsequent treatment, and the mixture of ferric hydroxi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B25/37C01B25/42
Inventor 叶瑛夏天秦雯丽夏枚生张平萍陈雪刚张维睿
Owner ZHEJIANG UNIV
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