Process for recovery of excess energy of flue gas from converter

A technology for steelmaking converter and waste energy recovery, which is applied in the improvement of process efficiency, furnace and furnace components, etc., can solve the problems of limited waste heat recovery, gas explosion, and difficulty in efficient utilization of steam, and achieves improved dust removal efficiency and extended service life. , the effect of reducing the possibility of gas explosion

Inactive Publication Date: 2007-05-30
昆明幸福阳光新能源有限公司
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AI Technical Summary

Problems solved by technology

[0002] When the steelmaking converter is in production, its specific steelmaking process makes it produce high-temperature flue gas intermittently. Therefore, although there is a certain recovery of the high-temperature energy contained in the high-temperature flue gas produced by it in the world , such as the process and method of reducing the temperature in the flue gas from 1400-1650 ° C to 800-1000 ° C through vaporization cooling heat exchange, but because the high-temperature flue gas generated is intermittent, waste heat recovery is limited and intermittent production Makes steam difficult to use efficiently
In addition, because the main components of high-temperature flue gas are carbon monoxide, carbon dioxide, some nitrogen and oxygen, and a large amount of dust, etc., in the gap production process, it is very easy to cause a gas explosion if it is not handled properly.

Method used

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  • Process for recovery of excess energy of flue gas from converter
  • Process for recovery of excess energy of flue gas from converter
  • Process for recovery of excess energy of flue gas from converter

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Embodiment Construction

[0017] The present invention will be further described below by way of examples, but not limited to examples.

[0018] Take the No. 6 steelmaking converter flue gas dry dust removal and residual energy recovery device of Kunming Steel No. 3 Steelmaking Plant as an example. Converter technical parameters:

[0019] 1. Converter nominal volume: 50t

[0020] 2. Average smelting cycle: 33min

[0021] 3. Oxygen blowing time: 14~17min

[0022] 4. Maximum furnace gas volume: 35600m 3 / h (standard condition)

[0023] 5. The temperature of the furnace gas outlet entering the fume hood: combustion period: 1400 ℃ ~ 1650 ℃ recovery period: 1200 ℃ ~ 1400 ℃

[0024] 6. Initial dust concentration: 80~150g / Nm 3 (standard condition)

[0025] 7. Dispersion of smoke and dust:

[0026] particle size / um

<0.5

0.5-1

1-2

2-10

10-40

>40

Combustion method / %

50

45

5

Unburned method / %

3...

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Abstract

The invention relates to gas residual energy recovery area of steelmaking converter, comprising eliminating dust for high-temperature gas generated in steelmaking converter, decreasing the temperature of recovery steam by heat exchanging, and collecting gas; characterized in that in not-blowing period of steelmaking converter, converter gas collected is returned to combustor between hood and vaporizing cooling flue and is mixed with air to burn; high temperature gas with more than 1500DEG C generated in vaporizing cooling flue can ensure steam recovery enough and continuously and control oxygen content in gas equal to or less than 1% after burning. The merit is that oxygen content of gas in flue is used in the process that burning decreases the gap of converter effectively, meanwhile residual energy recovery is continued, the safety and recovery efficiency of residual energy are improved greatly and the service life of equipment is prolonged. It is the effective method for decreasing steelmaking energy consumption.

Description

technical field [0001] The invention relates to the field of recovery of residual energy from flue gas of a steelmaking converter. Background technique [0002] When the steelmaking converter is in production, its specific steelmaking process makes it produce high-temperature flue gas intermittently. Therefore, although there is a certain recovery of the high-temperature energy contained in the high-temperature flue gas produced by it in the world , such as the process and method of reducing the temperature in the flue gas from 1400-1650 ° C to 800-1000 ° C through vaporization cooling heat exchange, but because the high-temperature flue gas generated is intermittent, waste heat recovery is limited and intermittent production Makes it difficult to use steam efficiently. In addition, because the main components of high-temperature flue gas are carbon monoxide, carbon dioxide, some nitrogen and oxygen, and a large amount of dust, etc., gas explosions are likely to occur if no...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F27D17/00
CPCY02P10/25
Inventor 刘连城耿加祥杨振立
Owner 昆明幸福阳光新能源有限公司
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