A kind of mica type stone coal extraction v <base:sub> 2</base:sub> o <base:sub> 5</base:sub> and kal(so <base:sub> 4</base:sub> ) <base:sub> 2</base:sub> 12h <base:sub> 2</base:sub> o's method

A 2·12H2O and stone coal technology, applied in the direction of improving process efficiency, can solve the problems of insignificant recovery of valuable element potassium and complicated process, and achieve high yield, simple operation, and improved crystallization rate.

Active Publication Date: 2017-08-08
WUHAN UNIV OF SCI & TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In this process, the concentration of potassium in the pickling solution is relatively low, adding potassium-rich materials can promote the crystallization of potassium aluminum sulfate, and potassium aluminum sulfate is transformed to obtain potassium-rich materials, and the potassium-rich materials can be added to the pickling solution to crystallize potassium aluminum sulfate. In the process of crystallization of aluminum potassium sulfate to prepare potassium-rich materials, it is necessary to continuously add chemicals to adjust the acidity, the process is complicated, and the recovery effect of the valuable element potassium is not significant

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] A kind of mica type stone coal extraction V 2 o 5 and KAl(SO 4 ) 2 12H 2 O's method. The concrete steps of described method are:

[0035] Step 1. Sulfation Roasting

[0036] Crush and grind mica-type stone coal raw ore to obtain mica-type stone coal; according to the mass ratio of mica-type stone coal and sulfuric acid to 1.0: (0.3~0.45), mix mica-type stone coal and sulfuric acid, and then Sulfate roasting at 200°C for 90-120 minutes to obtain calcined sand.

[0037] Step two, one stage leaching

[0038] Mix the calcined sand with the primary leaching agent at a solid-to-liquid ratio of 1.0︰(1.4~1.8) kg / L, and stir and leaching at 60~80°C for 20~50 minutes to obtain the ore pulp after the primary leaching.

[0039] Step 3, a stage of solid-liquid separation

[0040] The ore pulp after a stage of leaching is subjected to a stage of solid-liquid separation under the condition of 50-65°C to obtain a stage of leachate and a stage of leaching slag.

[0041] Step 4...

Embodiment 2

[0052] A kind of mica type stone coal extraction V 2 o 5 and KAl(SO 4 ) 2 12H 2 O's method. The concrete steps of described method are:

[0053] Step 1. Sulfation Roasting

[0054] Crush and grind mica-type stone coal raw ore to obtain mica-type stone coal; according to the mass ratio of mica-type stone coal and sulfuric acid to 1.0: (0.35~0.5), mix mica-type stone coal and sulfuric acid, and then Sulfate roasting at 300°C for 60-100 minutes to obtain calcined sand.

[0055] Step two, one stage leaching

[0056] Mix the calcined sand with the first-stage leaching agent at a solid-to-liquid ratio of 1.0: (1.0-1.5) kg / L, and stir and leaching at 65-85°C for 40-70 minutes to obtain the ore pulp after the first-stage leaching.

[0057] Step 3, a stage of solid-liquid separation

[0058] The ore pulp after one-stage leaching is subjected to one-stage solid-liquid separation under the condition of 60-75° C. to obtain one-stage leachate and one-stage leach slag.

[0059] St...

Embodiment 3

[0070] A kind of mica type stone coal extraction V 2 o 5 and KAl(SO 4 ) 2 12H 2 O's method. The concrete steps of described method are:

[0071] Step 1. Sulfation Roasting

[0072] Crush and grind mica-type stone coal raw ore to obtain mica-type stone coal; according to the mass ratio of mica-type stone coal and sulfuric acid to 1.0: (0.45~0.6), mix mica-type stone coal and sulfuric acid, and then Sulfate roasting at 220°C for 30-70 minutes to obtain calcined sand.

[0073] Step two, one stage leaching

[0074] Mix the calcined sand with the first-stage leaching agent at a solid-to-liquid ratio of 1.0:(0.7-1.2) kg / L, stir and leaching at 70-90°C for 60-90 minutes to obtain the ore pulp after the first-stage leaching.

[0075] Step 3, a stage of solid-liquid separation

[0076] The ore pulp after one-stage leaching is subjected to one-stage solid-liquid separation under the condition of 65-80°C to obtain one-stage leachate and one-stage leach slag.

[0077] Step 4, tw...

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Abstract

The invention particularly relates to a method for extracting V2O5 and KAl(SO4)2.12H2O from mica-type stone coal. The technical scheme is as follows: the method comprises the following steps: crushing mica-type stone coal raw ore, grinding, and carrying out sulfating roasting to obtain a roasted product; carrying out primary leaching and primary solid-liquid separation on the roasted product to obtain a primary leach solution and a primary leach residue; carrying out secondary leaching on the primary leach residue, carrying out secondary solid-liquid separation to obtain a secondary leach solution and a secondary leach residue, returning the secondary leach solution as a primary leaching agent, and using the secondary leach residue as end tailings; cooling the primary leach solution to crystallize to obtain a crude product and a mother solution, and recrystallizing the crude product to obtain the KAl(SO4)2.12H2O; and extracting the mother solution to obtain an extraction raffinate and a vanadium-rich solution, returning the extraction raffinate as a secondary leaching agent, and precipitating vanadium from the vanadium-rich solution to obtain the product V2O5. The method has the characteristics of high V and K leaching rates, high yield, high production continuity and environment friendliness, and is simple to operate.

Description

technical field [0001] The invention belongs to the technical field of mica type stone coal. Especially relate to a kind of mica type stone coal extraction V 2 o 5 and KAl(SO 4 ) 2 12H 2 O's method. Background technique [0002] Potassium resource reserves in my country are small, unevenly distributed and low self-sufficiency rate. At present, the potassium minerals that have been developed and utilized are mainly brine potassium ore, which cannot meet the needs of our country. Insoluble potassium-containing minerals (mica, potassium feldspar, alunite, etc.) have not been fully utilized due to their low grade and high economic cost of independent development. [0003] Stone coal is a unique vanadium-containing resource in my country. Most vanadium in stone coal exists in mica-like aluminosilicate minerals. When V is extracted from stone coal, the structure of silicate minerals is destroyed, and the valuable element K With V into the leachate and be enriched. Product ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/04C22B3/26C22B26/10C22B34/22
CPCY02P10/20
Inventor 张一敏师启华艾军郝文彬刘涛黄晶
Owner WUHAN UNIV OF SCI & TECH
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