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Device for producing high-activity magnesium oxide by using magnesite tailings

A magnesia device and magnesite tailings technology, applied in the field of refractory material production, can solve the problems of waste of resources, secondary pollution, and dust leakage to pollute the environment, and achieve stable product quality, controllable feeding speed, and working environment. cleaning effect

Active Publication Date: 2017-11-07
LIAONING DONGHE NEW MATERIAL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, the commonly used traditional equipment for the production of high-activity magnesia in my country includes light-fired shaft kilns, rotary kilns, fluidized fluidized kilns, suspension roasters, multi-layer roasters, and reverberatory kilns, all of which have requirements for the structure of calcined minerals, and the sieved powder The shape cannot be reused in the kiln, which wastes resources. The calcination time of uneven lumps and small particles entering the kiln is not properly controlled, and it is prone to under-burning or over-burning. The process dust leaks and pollutes the environment. The hydration activity is unstable. Fine grinding and grading, the follow-up process is prone to moisture absorption and secondary pollution, and the product is low and of poor quality
The above equipment has serious defects, making it difficult to complete the high-value utilization of tailings and off-grade powder ore, resulting in waste of resources, serious damage to the environment, and difficulty in meeting the requirements of environmental protection, energy saving and emission reduction, and reducing operating costs.

Method used

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  • Device for producing high-activity magnesium oxide by using magnesite tailings

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Effect test

Embodiment 1

[0026] A production process for producing a high-activity magnesium oxide device using magnesite tailings, specifically comprising the following steps:

[0027] 1) After the magnesite tailings flotation, the concentrate powder is mixed with the recovered magnesium oxide powder, the concentrate powder MgO content is 42-43%, the recovered magnesium oxide powder MgO content is greater than 95-97.5%, the concentrate powder and the recovered magnesium oxide powder The ratio is 6.5:1;

[0028] 2) The wet material is continuously conveyed into the flash dryer through the filter cake feeder. Under the joint action of the main rotating blade and the high-speed hot air flow, the wet material is quickly dispersed into powder, which expands the evaporation area. High-speed mass transfer and heat transfer, instantly vaporize and evaporate water molecules, dry and dehydrate to ≤1-0.5%, and the materials that meet the requirements of restoring original particle size and moisture enter the fi...

Embodiment 2

[0032] A production process for producing a high-activity magnesium oxide device using magnesite tailings, specifically comprising the following steps:

[0033] 1) After the magnesite tailings flotation, the concentrate powder is mixed with the recovered magnesium oxide powder, the concentrate powder MgO content is 43-44%, the recovered magnesium oxide powder MgO content is greater than 95-96%, the concentrate powder and the recovered magnesium oxide powder The ratio is 7:1;

[0034] 2) The wet material is continuously conveyed into the flash dryer through the filter cake feeder. Under the joint action of the main rotating blade and the high-speed hot air flow, the wet material is quickly dispersed into powder, which expands the evaporation area. High-speed mass transfer and heat transfer, instantly vaporize and evaporate water molecules, dry and dehydrate to ≤1-0.5%, and the materials that meet the requirements of restoring original particle size and moisture enter the first ...

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Abstract

The invention relates to a device for producing high-activity magnesium oxide by using magnesite tailings. The device comprises a gas-fired hot air furnace, a filter cake feeder, a flash vaporization drier, cyclone separators, bag-type dust collectors, a preheater, a screw feeder, a flash cyclone dynamic calciner, a gas-solid separator, a clinker silo, an air cooling system and a product stock bin, wherein the gas-fired hot air furnace is connected with the filter cake feeder; the filter cake feeder is connected with the flash vaporization drier; an outlet of the flash vaporization drier is connected with the first cyclone separator and the first bag-type dust collector; the first bag-type dust collector is connected with the preheater; the preheater is connected with the flash cyclone dynamic calciner through the screw feeder; an outlet of the flash cyclone dynamic calciner is connected with the gas-solid separator; the gas-solid separator is respectively connected with the clinker silo and the second bag-type dust collector; the clinker silo is connected with the air cooling system; the air cooling system is connected with the second cyclone separator and the second bag-type dust collector; the second bag-type dust collector is connected with the product stock bin; the flash cyclone dynamic calciner introduces waste heat into the flash vaporization drier.

Description

technical field [0001] The invention relates to the production of refractory materials, in particular to a device for producing high-activity magnesium oxide by utilizing magnesite tailings. Background technique [0002] There are very few good-grade magnesites with a magnesium oxide (MgO) content of more than 46.5% in my country. A large number of low-grade ores and crushed magnesite need to be fully utilized. [0003] At present, the commonly used traditional equipment for the production of high-activity magnesia in my country includes light-fired shaft kilns, rotary kilns, fluidized fluidized kilns, suspension roasters, multi-layer roasters, and reverberatory kilns, all of which have requirements for the structure of calcined minerals, and the sieved powder The shape cannot be reused in the kiln, which wastes resources. The calcination time of uneven lumps and small particles entering the kiln is not properly controlled, and it is prone to under-burning or over-burning. T...

Claims

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Application Information

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IPC IPC(8): C04B2/10
CPCC04B2/102C04B2/104Y02P40/40
Inventor 毕胜民吴国华董宝华孙希忠赵权秦楠钟刚王飞石生凯王新星肖立宏王耶
Owner LIAONING DONGHE NEW MATERIAL CO LTD
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