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Method for preparing carbonyl iron through medium pressure continuous gasification

A carbonyl iron, medium-pressure technology, which is applied in the field of medium-pressure continuous gasification to prepare carbonyl iron, can solve the problems of low production efficiency and long auxiliary time.

Inactive Publication Date: 2014-04-16
JINCHUAN GROUP LIMITED
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Both the high-pressure production process and the medium-pressure production process have the problems of long auxiliary time and low production efficiency in practical operation, and the auxiliary time accounts for about 30% of the annual production period

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] The ferroalloy powder is controlled to enter the bottom of the synthesis kettle at a feed rate of 50kg / h, and the 7MPa CO gas is heated to 150°C at a feed rate of 1000NM3 / h and then passed into the bottom of the synthesis kettle. The primary copper-iron alloy powder flows upward from the bottom driven by the CO gas flow. The mixed gas obtained at the top of the continuous synthesis kettle is passed through the dust collector, and the primary ferroalloy reaction residue is obtained at the bottom of the dust collector. The mixed gas drawn from the top of the dust collector passes through the gas heat exchanger and condenser to obtain carbonyl iron liquid and CO gas containing a small amount of carbonyl iron. After the mixed gas passes through the pyrolysis device, a small amount of carbonyl iron powder and pure CO gas are obtained. CO gas is sent into the synthesis kettle through a gas compressor to re-participate in the continuous carbonyl carbonylation reaction of iron c...

Embodiment 2

[0016] The ferroalloy powder is controlled to enter the bottom of the synthesis kettle at a feeding rate of 80kg / h. 8MPa CO gas is heated to 180°C at a feeding rate of 1500NM3 / h and then passed into the bottom of the synthesis kettle. The ferroalloy powder flows upward from the bottom driven by the CO gas flow. The mixed gas obtained from the top of the continuous synthesis kettle is passed through the dust collector, and the ferroalloy reaction residue is obtained at the bottom of the dust collector. The mixed gas drawn from the top of the dust collector passes through the gas heat exchanger and condenser to obtain carbonyl iron liquid and CO gas containing a small amount of carbonyl iron. After the mixed gas passes through the pyrolysis device, a small amount of carbonyl iron powder and pure CO gas are obtained. CO gas is sent into the synthesis kettle through a gas compressor to re-participate in the continuous carbonylation reaction of carbonyl iron, and the reaction ends a...

Embodiment 3

[0018] The ferroalloy powder is controlled to enter the bottom of the synthesis kettle at a feeding rate of 120kg / h. 8Mpa CO gas is heated to 180°C at a feeding rate of 1500NM3 / h and then passed into the bottom of the synthesis kettle. The ferroalloy powder flows upward from the bottom driven by the CO gas flow. The mixed gas obtained from the top of the continuous synthesis kettle is passed through the dust collector, and the ferroalloy reaction residue is obtained at the bottom of the dust collector. The mixed gas drawn from the top of the dust collector passes through the gas heat exchanger and condenser to obtain carbonyl iron liquid and CO gas containing a small amount of carbonyl iron. After the mixed gas passes through the pyrolysis device, a small amount of carbonyl iron powder and pure CO gas are obtained. CO gas is sent into the synthesis kettle through a gas compressor to re-participate in the continuous carbonyl carbonylation reaction of iron carbonyl, and the react...

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PUM

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Abstract

The invention discloses a method for preparing carbonyl iron through medium pressure continuous gasification, and relates to a method for continuously preparing carbonyl iron from an iron alloy material in a fluidized bed synthetic kettle. The method is characterized in that during the preparation process, iron alloy powder and heated CO are led in from the bottom of the synthetic kettle; the iron alloy powder is driven to flow upwards by CO flow; during the rising process, the iron alloy powder is in reaction with high-temperature CO to obtain carbonyl iron gas; the reaction residue and mixed gas of CO and the carbonyl iron are discharged from the top; the reaction residue is obtained via a separation and dust collecting device; the mixed gas of CO and carbonyl iron is cooled and separated to respectively obtain a carbonyl iron liquid and the mixed gas containing carbonyl iron and CO; carbonyl iron powder and pure CO are prepared from the mixed gas via a pyrolysis device; CO returns to the bottom of the synthetic kettle to be involved in the reaction; the whole production is a long period continuous process. The continuous reaction is realized.

Description

technical field [0001] The invention discloses a method for preparing carbonyl iron by medium-pressure continuous gasification, which relates to a method for continuously preparing carbonyl iron from ferroalloy materials in a fluidized bed synthesis kettle. Background technique [0002] The carbonyl iron refining process uses carbon monoxide and metallic iron to react under a certain temperature and pressure to form a metal carbonyl compound, and then pyrolyzes the metal carbonyl compound to obtain a method of pure metal. The carbonyl method of refining iron is not only simple in process, low in energy consumption and high in extraction rate, but also beneficial to the enrichment of precious metals. It is an environmentally friendly process without three wastes. Its products such as iron powder and alloy powder are widely used new materials. [0003] There are currently three industrial carbonyl iron synthesis processes: atmospheric pressure carbonyl method, medium pressure...

Claims

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Application Information

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IPC IPC(8): C01G49/16
Inventor 王芳镇肖冬明禹松涛江龙刘军位罗世铭刘俊甘振君
Owner JINCHUAN GROUP LIMITED
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