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Double-calcination process of sulfuric acid and rare earth concentrate rotary kiln calcination device

A rare earth sulfate, roasting device technology, applied in waste heat treatment, lighting and heating equipment, furnace components and other directions, can solve the problems of difficult waste gas treatment technology, high investment and operating costs, waste of radioactive thorium resources, etc. The effect of processing, improving the utilization rate of heat energy and improving the utilization rate of resources

Active Publication Date: 2013-12-04
LUOYANG CEMENT ENG DESIGN & RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The main defects of this process are: (1) thorium exists in the waste residue in the form of pyrophosphate, which cannot be recycled, causing the waste of thorium resources to exceed the standard; (2) a large amount of waste gas is produced at the kiln tail, and the waste gas contains HF, SO 2 , SO 3 , sulfuric acid mist and other harmful components, resulting in difficult waste gas treatment technology, complex process, high investment and operating costs, in view of the above reasons, it is necessary to improve the device and roasting process of rare earth concentrate roasting kiln

Method used

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  • Double-calcination process of sulfuric acid and rare earth concentrate rotary kiln calcination device

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] As shown in the figure; the outlet end of the low-temperature roasting kiln 13 is set above the inlet end of the high-temperature roasting kiln 17, the feed smoke chamber 12 is set at the inlet end of the low-temperature roast kiln 13, the inlet is arranged above the feed smoke chamber 12, and the top of the feed smoke chamber 12 Set the feeding system, the dry powder bin 8 is set under the gas-solid separator 7 of the low temperature system of the feeding system, the dry powder metering scale 9 is set under the outlet of the dry powder bin 8, and the agitator 10 is set under the dry powder metering scale 9, and the agitator 10- A sulfuric acid metering system 11 is installed on the side, and a pipeline is arranged between the agitator 10 and the sulfuric acid metering system 11. The lower part of the outlet of the agitator 10 corresponds to the inlet of the low-temperature roasting kiln 13 feeding fume chamber 12; the side of the feeding fume chamber 12 inlet A dispersi...

Embodiment 2

[0039] As shown in the figure; low-temperature kiln combustion system 14 is set in the middle of the outlet end of low-temperature roasting kiln 13, high-temperature kiln combustion system 18 is set in the middle of the outlet end of high-temperature roasting kiln 17, and smoke is set between the outlet end of high-temperature roasting kiln 17 and the outlet end of low-temperature roasting kiln 13. Gas discharge pipeline; the outlet of the low-temperature roasting kiln 13 is corresponding to the import of the high-temperature roasting kiln 17 to set the material pipeline, and the side of the high-temperature roasting kiln 17 inlet is provided with a high-temperature system gas-solid separator 20, and the delivery nozzle above the high-temperature roasting kiln 17 inlet is connected to the high-temperature Pipelines are arranged between the gas-solid separators 20 of the system; an inlet is arranged below the inlet side of the high-temperature roasting kiln 17, and an outlet is a...

Embodiment 3

[0040] The roasting temperature of the low-temperature roasting kiln 13 of the rotary kiln roasting rare earth concentrate of sulfuric acid in the present invention is between 200°C and 500°C. After ~450°C, it is discharged into the high-temperature nozzle above the dispersing dryer 6 through the pipeline, and the waste gas entering the dispersing dryer 6 through the high-temperature nozzle is dispersed and suspended for heat exchange with rare earth and iron powder. A pipeline is set between another conveying nozzle on the top and the gas-solid separator 7 of the low-temperature system. When the rare earth and iron powder in the dryer 6 are dispersed to become suspended solids, they enter the gas-solid separator 7 of the low-temperature system through the pipeline for gas-solid separation. Solid separation, the separated gas enters the low-temperature system dust collector 15 through the pipeline above the low-temperature system gas-solid separator 7 for dust removal, and the ...

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Abstract

The invention provides a sulfuric acid and rare earth concentrate rotary kiln calcination device. The device is characterized in that burnt waste gases of a high-temperature calcining kiln of a calcining kiln burning system are emitted to a low-temperature calcining kiln via a flue gas emission pipeline and the waste heat of the waste gases is reutilized; burnt waste gases of the low-temperature calcining kiln are emitted to a scattering dryer and the waste heat of the waste gases is reutilized; waste gases in the scattering dryer are emitted after undergoing gas-solid separation; waste gases at the inlet of the high-temperature calcining kiln are emitted after undergoing gas-solid separation; sulfuric acid and rare earth concentrate calcining materials of a calcining kiln system are calcined in the low-temperature calcining kiln and enter the inlet end of the high-temperature calcining kiln via the outlet end; and the calcining materials are calcined in the high-temperature calcining kiln and are discharged into a dissolving tank via a discharge pipe on one side of a cooling machine. The device has the following beneficial effects that the rare earth concentrate is subjected to full calcination at low temperature and at high temperature respectively, thus improving decomposition of the rare earth concentrate; the waste heat of the calcining kilns is recycled; the sulfuric acids in the recovered waste gases are used for production; the waste residues are reduced and the air is purified; and the device has strong process continuity, high degree of automation and low labor intensity and improves production.

Description

technical field [0001] The invention relates to a rare earth concentrate roasted by a rotary kiln, in particular to a secondary roasting process of a rotary kiln roasting device for a rare earth sulfate concentrate. Background technique [0002] Since the 1970s, my country began to develop the use of concentrated sulfuric acid roasting method to smelt Baotou mixed rare earth concentrates, and successively developed the first, second and third generation sulfuric acid methods, among which concentrated sulfuric acid high-temperature intensive roasting method (third-generation acid method) It has been put into use since the 1980s and has become the leading industrial production technology for processing Baotou rare earth concentrates. At present, 90% of Baotou rare earth concentrates are processed by concentrated sulfuric acid high-temperature intensified roasting. [0003] Concentrated sulfuric acid high temperature intensified roasting method (third-generation acid method) mai...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B1/06C22B59/00F27B19/04F27D17/00
Inventor 赵迎朝代家聚王群红陈辉魏军魁缪祥来
Owner LUOYANG CEMENT ENG DESIGN & RES INST
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