Direct reduction process for producing sponge iron by using CH4 non-catalytic oxygen-enriched transformation

A non-catalytic, sponge iron technology, applied in the field of iron or steel smelting, can solve the problems of long process flow, easy bonding of sponge iron, short service life of burners, etc., achieving strong controllability of process parameters, obvious investment and emissions , the effect of prolonging the service life

Active Publication Date: 2015-01-28
CISDI ENG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] 1) Use the coke oven gas and the purified and decarburized shaft furnace top gas together, humidify and then heat to about 1000°C and enter the shaft furnace to reduce iron ore. The key to this technical route is to use high temperature and the catalytic effect of sponge iron. make part of ch 4 A reforming reaction occurs to generate CO+H 2 Supplement reducing gas, but this process requires decarburization and oxygen spraying to raise temperature. At the same time, at a temperature of about 1000 ° C, if the reducing gas atmosphere is not well controlled, there will be defects that sponge iron is easy to stick;
[0006] 2) Use oxygen, coke oven gas, carbon dioxide, and water vapor to convert in the reformer, then mix with top gas, heat up to 800°C after desulfurization and decarburization, and enter the shaft furnace to reduce iron ore. At the same time, H 2 /CO>1.5; the process

Method used

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  • Direct reduction process for producing sponge iron by using CH4 non-catalytic oxygen-enriched transformation

Examples

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Example Embodiment

[0046] Example 1:

[0047] Sponge iron made from titanium vanadium magnetite

[0048] Coke oven gas is purified and pressurized as rich CH 4 The raw material gas and oxygen-enriched air are respectively preheated by the tubular heating furnace, rich in CH 4 The raw material gas is preheated to 400°C, and the oxygen-enriched air is preheated to 250°C; after the preheating, the two gases enter the non-catalytic oxygen-enriched reformer to undergo combustion reaction and heat up, and the CH 4 Converted into CO and H 2 , Forming a high-temperature conversion gas with a temperature of 1340℃.

[0049] At the same time as the above, the top gas from the shaft furnace that produces sponge iron is cooled to 210°C by the heat exchanger, enters the scrubbing tower, is washed to remove dust and cooled to 40°C, then pressurized to 0.45MPa by the press, and then enters the vacuum The pressure swing adsorption hydrogen purification device (VPSA) produces purified hydrogen with a purity of more than...

Example Embodiment

[0054] Example 2

[0055] Reduce ordinary iron ore to make sponge iron

[0056] Natural gas is purified and pressure-regulated as rich CH 4 The raw material gas and oxygen-enriched air are respectively preheated by the tubular heating furnace, rich in CH 4 The raw material gas is preheated to 350°C, and the oxygen-enriched air is preheated to 260°C; after the preheating, the two gases enter the non-catalytic oxygen-enriched reformer to undergo combustion reaction and heat up, and the CH 4 Converted into CO and H 2 , The formation temperature is 1350℃ high temperature conversion gas.

[0057] At the same time as the above, the top gas from the shaft furnace that produces sponge iron is cooled to 210°C by the heat exchanger, enters the scrubbing tower, is washed with water, and the temperature is reduced to 40°C, and then pressurized to 0.8MPa by the press before entering the vacuum The pressure swing adsorption hydrogen purification device (VPSA) produces purified hydrogen with a puri...

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Abstract

The invention relates to a direct reduction process for producing sponge iron by using CH4 non-catalytic oxygen-enriched transformation. A process route comprises the following steps: preheating a CH4-enriched raw gas and oxygen-enriched air which are subjected to purification and pressure regulation, then introducing the CH4-enriched raw gas and the oxygen-enriched air into a non-catalytic oxygen-enriched transformation furnace for a combustion reaction in the non-catalytic oxygen-enriched transformation furnace, and raising the temperature to transform CH4 therein into CO and H2 to form a high-temperature transformation gas; in the meantime, cooling, dedusting and pressurizing a top gas of a shaft furnace, then introducing the top gas into a hydrogen purification device to prepare purified hydrogen, preheating the purified hydrogen, and then introducing the preheated purified hydrogen into the lower part of the catalyst oxygen-enriched transformation furnace to be mixed with the high-temperature transformation gas generated through the combustion reaction to form a reduced coal gas; and introducing the reduced coal gas into the shaft furnace to reduce iron ores into the sponge iron. The direction reduction process disclosed by the invention not only has the advantages of short process flow, availability for energy saving and emission reduction, long service life of a nozzle and low investment cost, and can be used to prevent the sponge iron from caking and avoid carbon formation.

Description

technical field [0001] The present invention relates to a method utilizing CH 4 The invention relates to a direct reduction process for producing sponge iron by non-catalytic oxygen-enriched transformation, which belongs to the technical field of iron or steel smelting. Background technique [0002] The iron and steel industry is the basic industry of the national economy, and it is also a key industry in my country's energy resource consumption and pollution discharge. In order to speed up structural adjustment and industrial upgrading of the iron and steel industry, change the development mode of the iron and steel industry, and promote economical, clean and sustainable development, the state proposed in the "Steel Industry Adjustment and Revitalization Plan" to "strengthen non-blast furnace smelting-steelmaking, refining-direct Rolling new process clean process technology research and development and testing" as a key task to promote energy conservation and emission redu...

Claims

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Application Information

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IPC IPC(8): C21B13/02
CPCY02P10/143
Inventor 郭敏李佳楣吴开基张涛赵运建
Owner CISDI ENG CO LTD
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