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A kind of slag iron graphite separation and purification process

A technology of graphite and slag iron, applied in the direction of inorganic chemistry, non-metallic elements, carbon compounds, etc., can solve the problems of cumbersome process, high cost, and environmental pollution by flotation agents, and achieve the goal of reducing cost, simplifying process, and pollution-free environment Effect

Inactive Publication Date: 2017-07-04
王太进
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Background technology mostly uses strong acid for recycling, which pollutes the environment; Chinese patent application 2015103120211, titled "a method for recovering flake graphite from molten iron desulfurization slag", the specific steps of the method are: firstly, the desulfurization slag is broken, and the iron is recovered by magnetic separation , the tailings are crushed to less than 1mm and water is added to make a slurry with a concentration of 30-40%, and the flotation agent is added into the flotation machine for flotation, and the scum is added with water to make a slurry with a concentration of 50-70% and ball milled for 10-30min, then Iron is recovered by magnetic separation, and the tailings are added with water to make a slurry with a concentration of 30-50%, which is sent to a flotation machine for flotation. The flotation agent is "kerosene + No. 2 flotation oil" or "liquid paraffin + octanol" Composition, the recycled flake graphite is processed through multiple "ball milling-magnetic separation-flotation" processes to improve the grade, and the fixed carbon content in the finally obtained flake graphite can reach more than 90%; The agent also has the problem of polluting the environment, and the fixed carbon content in flake graphite is low

Method used

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  • A kind of slag iron graphite separation and purification process
  • A kind of slag iron graphite separation and purification process

Examples

Experimental program
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Effect test

Embodiment 1

[0028] The desulfurization slag is crushed and sieved firstly, and then primary selection is carried out by overflow stirring to remove suspended impurities, and the fixed carbon content of the material is 68%;

[0029] Then the material enters the shaking table for selection, and the number of shaking tables is two; adjust the parameters of the shaking table according to the change of the fixed carbon content in the material; if the fixed carbon content of the material entering the shaking table is low, reduce the tilt angle of the shaking table, Flatten the bed surface and reduce the water volume of the shaker; if the fixed carbon content of the material entering the shaker is high, increase the tilt angle of the shaker to make the bed surface inclined and increase the water volume of the shaker;

[0030] After being selected, the material enters the immersion tank, and the liquid containing acetate is added to the immersion tank to react with calcium oxide, magnesium c...

Embodiment 2

[0033] The desulfurization slag is first crushed and sieved, and then overflowed and stirred for primary selection to remove suspended impurities. The fixed carbon content of the material is 72%;

[0034] Then the material enters the shaking table for selection, and the number of shaking tables is two; adjust the parameters of the shaking table according to the change of the fixed carbon content in the material; if the fixed carbon content of the material entering the shaking table is low, reduce the tilt angle of the shaking table, Flatten the bed surface and reduce the water volume of the shaker; if the material entering the shaker has a high fixed carbon content, increase the tilt angle of the shaker to make the bed surface inclined and increase the water volume of the shaker;

[0035] After being selected, the material enters the soaking tank, and the liquid containing acetate is added to the soaking tank to react with the calcium oxide, magnesium chloride and aluminu...

Embodiment 3

[0038] The desulfurization slag is crushed and sieved firstly, and then primary selection is carried out by overflow stirring to remove suspended impurities, and the fixed carbon content of the material is 70%;

[0039] Then the material enters the shaking table for selection, and the number of shaking tables is two; adjust the parameters of the shaking table according to the change of the fixed carbon content in the material; if the fixed carbon content of the material entering the shaking table is low, reduce the tilt angle of the shaking table, Flatten the bed surface and reduce the water volume of the shaker; if the fixed carbon content of the material entering the shaker is high, increase the tilt angle of the shaker to make the bed surface inclined and increase the water volume of the shaker;

[0040] After being selected, the material enters the immersion tank, and the liquid containing acetate is added to the immersion tank to react with calcium oxide, magnesium ch...

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Abstract

The invention relates to a slag iron graphite separating and purifying process, and belongs to the technical field of graphite recycle from slag iron. According to the technical scheme, the process comprises the following steps: firstly conducting crushing and screening on desulfurated slag, then conducting overflow stirring primary selection, and then putting the material (namely, the processed slag) into a shaking table for fine selection; putting the finely selected material into a soaking tank, adding an acetate contained liquid into the soaking tank, conducting reaction on the acetate contained liquid and calcium oxide, magnesium chloride and aluminium oxide in the desulfurated slag, and further removing impurities; finally conducting spin-drying and stoving on the material to obtain the graphite finished product. The process has the advantages that active effects that the fixed carbon content of the slag iron material subjected to crushing and screening (1) and overflow stirring primary selection (2) is 65-75%, and the fixed carbon content of the finished product subjected to shaking table fine selection (3), treatment by adding the acetate contained liquid into the soaking tank (4), spin-drying (5) and stoving (6) is 93% or above. The acetate contained liquid is added for treating the slag iron, so that environment pollution can be avoided; the process is simplified, the cost is reduced, the environment pollution problem is avoided, and the fixed carbon content of the flake graphite is relatively high.

Description

technical field [0001] The invention relates to a process for separating and purifying slag-iron-graphite, in particular to a method for recovering flake graphite from desulfurization slag produced during desulfurization in iron and steel production, and belongs to the technical field of graphite recovery from slag-iron. Background technique [0002] In iron and steel production, a large amount of desulfurization slag, referred to as slag iron, will be produced during the desulfurization process of molten iron; slag iron will be mixed with flake graphite, which is easy to float and cause environmental pollution. Background technology mostly uses strong acid for recycling, which pollutes the environment; Chinese patent application 2015103120211, titled "a method for recovering flake graphite from molten iron desulfurization slag", the specific steps of the method are: firstly, the desulfurization slag is broken, and the iron is recovered by magnetic separation , the tailings ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B32/215
Inventor 王太进
Owner 王太进
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