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Method for extracting V2O5 and KAl(SO4)2.12H2O from mica-type stone coal

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

Active Publication Date: 2015-07-22
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] One kind of cloud -mother stone coal extract V 2 O 5 And kal (so 4 Cure 2 · 12H 2 O method.The specific steps of the method are:

[0035] Step 1. Sulfuric acid baking

[0036] Broken and grind the raw ore of Yunmu -type stone coal to obtain Yunmu type stone coal; according to the quality ratio of Yunmu -type stone coal to sulfuric acid, 1.0: (0.3 ~ 0.45), mix the cloud -mother stone coal with sulfuric acid, and then at 120 ~Under the condition of 200 ° C, sulfuric acid is 90 ~ 120 min to get roasted sand.

[0037] Step 2, one stage immersion

[0038] Mix the baked sand from a section of leaching agent to 1.0: (1.4 ~ 1.8) kg / L, mix it at 60 ~ 80 ° C for 20 ~ 50 minutes, and obtain a section of mowing pulp.

[0039] Step 3, one section of solid fluid separation

[0040] A section of the pulp after a section of immersed is separated at 50 ~ 65 ° C to obtain a section of immersion liquid and a section of immersion residue.

[0041] Step 4, 2 stage immersion

[0042] The first l...

Embodiment 2

[0052] One kind of cloud -mother stone coal extract V 2 O 5 And kal (so 4 Cure 2 · 12H 2 O method.The specific steps of the method are:

[0053] Step 1. Sulfuric acid baking

[0054] Break the Yunmu -type stone coal ore, grind the ore, and get the cloud -mother stone coal; according to the quality ratio of Yunmu type stone coal to 1.0: (0.35 ~ 0.5), mix the cloud mother stone coal with sulfuric acid, and then at 180 ~ 180 ~Under 300 ° C, sulfuric acid is roasted for 60 ~ 100 min to get roasted sand.

[0055] Step 2, one stage immersion

[0056] Mix the baked sand from a section of leaching agent to 1.0: (1.0 ~ 1.5) kg / L, mix it at 65 ~ 85 ° C for 40 ~ 70 minutes, and get a section of the pulp after an leaching.

[0057] Step 3, one section of solid fluid separation

[0058] A section of the pulp after a section of immersed is separated at 60 ~ 75 ° C to obtain a section of immersion liquid and a section of immersion residue.

[0059] Step 4, 2 stage immersion

[0060] The first le...

Embodiment 3

[0070] One kind of cloud -mother stone coal extract V 2 O 5 And kal (so 4 Cure 2 · 12H 2 O method.The specific steps of the method are:

[0071] Step 1. Sulfuric acid baking

[0072] Broken and grind the raw ore of Yunmu -type stone coal to obtain Yunmu type stone coal; according to the quality ratio of cloud -type stone coal to sulfuric acid, 1.0: (0.45 ~ 0.6), mix the cloud -mother stone coal with sulfuric acid, and then in 150 ~Under the condition of 220 ° C, sulfuric acid is roasted for 30 ~ 70 min to get roasted sand.

[0073] Step 2, one stage immersion

[0074] Mix the baked sand from a section of leaching agent to 1.0: (0.7 ~ 1.2) kg / L, mix it at 70 ~ 90 ° C for 60 ~ 90min, and get a section of the pulp after an leaching.

[0075] Step 3, one section of solid fluid separation

[0076] A section of the pulp after a section of immersed is separated at 65 ~ 80 ° C to obtain a section of immersion liquid and a section of immersion residue.

[0077] Step 4, 2 stage immersion

...

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PUM

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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 field of Yunmu -type stone coal technology.Especially involved a kind of cloud -mother stone coal extraction V 2 O 5 And kal (so 4 Cure 2 · 12H 2 O method. Background technique [0002] my country's potassium resource reserves are small, the distribution is uneven, and the self -sufficiency rate is low.At present, the potassium minerals that have been developed and used are mainly brine potassium ore, which cannot meet my country's needs.Due to the low quality of potassium containing potassium minerals (cloud mother, potassium long stone, alum stone, etc.), the high cost of developing economic costs has not been fully utilized. [0003] Stone coal is a unique type of puppet resource in my country. Most of the stone coal is existed in cloudmate aluminum silicate minerals. While extracting V from the stone coal, the silicate mineral structure is destroyed. Enter the immersion solution with V and be enriched.Product V only extracts...

Claims

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Application Information

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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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