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A Smelting Reduction Ironmaking Method Partially Substituting Pure Oxygen

A pure oxygen, melter gasifier technology, applied in furnace types, furnaces, shaft furnaces, etc., can solve the problems of easy bonding of shaft furnaces, large coke usage, gas back-channeling, etc., to reduce the cost of pure oxygen consumption, The effect of improving the reduction metallization rate and reducing the CO2 content

Active Publication Date: 2017-10-31
BAOSHAN IRON & STEEL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] From the perspective of production, the smelting reduction process has problems such as poor air permeability of the shaft furnace, easy bonding of the shaft furnace, a large number of damages to the tuyere, blockage of the riser pipe, backflow of gas, blockage of the surrounding pipe of the shaft furnace, and large coke usage. These problems often lead to problems such as factory shutdown, low production utilization, etc., which lead to increased production costs

Method used

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  • A Smelting Reduction Ironmaking Method Partially Substituting Pure Oxygen

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] see figure 1 , the smelting reduction ironmaking method that partially replaces pure oxygen in the present invention, it passes the furnace top gas with a temperature of 250°C from the reduction shaft furnace 1 into the hot cyclone dust collector 3, and enters the heat exchange device 5 after being dedusted by the hot cyclone During heat exchange with 0.2MPa saturated steam, the saturated steam after the heat exchange becomes supersaturated steam at a temperature of 150°C, and the supersaturated steam is injected into the melter-gasifier 2 from the tuyere with an injection volume of 20Nm 3 / tHM, while injecting pure oxygen into other tuyeres, the amount of pure oxygen is 530Nm 3 / tHM. See Table 1 for the content of each component in the reduced gas coming out of the melter-gasifier 2 after the reaction in the melter-gasifier 2 . The reduced gas produced in the melter-gasifier 2 is mixed with cold gas and then enters the hot cyclone dust collector 3. The gas is divided...

Embodiment 2

[0026] The furnace top gas with a temperature of 280°C from the reduction shaft furnace 1 is passed into the hot cyclone dust collector 3, and after being dedusted by the hot cyclone, it enters the heat exchange device 5, and exchanges heat with 0.22MPa saturated steam. Saturated steam becomes supersaturated steam at a temperature of 170°C, and the supersaturated steam is sprayed into the melter-gasifier 2 from the tuyere with an injection volume of 30Nm 3 / tHM, while injecting pure oxygen into other tuyeres, the amount of pure oxygen is 520Nm 3 / tHM. See Table 1 for the content of each component in the reduced gas coming out of the melter-gasifier 2 after the reaction in the melter-gasifier 2 . The reduced gas produced in the melter gasifier 2 is mixed with cold gas and then enters the hot cyclone dust collector 3. The gas is divided into two paths, one path enters the reduction shaft furnace 1 at a temperature of 820°C, and the other path enters the scrubber 4 after washing...

Embodiment 3

[0028] The furnace top gas with a temperature of 300°C from the reduction shaft furnace 1 is passed into the hot cyclone dust collector 3, and after being dedusted by the hot cyclone, it enters the heat exchange device 5, and exchanges heat with 0.25MPa saturated steam. The saturated steam becomes supersaturated steam, the temperature is 180°C, and the supersaturated steam is sprayed into the melting and gasification furnace 2 from the tuyere, and the injection volume is 40Nm 3 / tHM, while injecting pure oxygen into other tuyeres, the amount of pure oxygen is 500Nm 3 / tHM. See Table 1 for the content of each component in the reduced coal gas coming out of the melter-gasifier 1 after the reaction in the melter-gasifier 1 . The reduced gas produced in the melter-gasifier 1 is mixed with cold gas and then enters the hot cyclone dust collector 3. The gas is divided into two paths, one path enters the reduction shaft furnace 1 at a temperature of 830°C, and the other path enters th...

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Abstract

The invention discloses a smelting reduction ironmaking method which partially replaces pure oxygen. The reduced metallization rate of smelting reduction direct reduced iron is not high, and the furnace top gas cannot be fully utilized, so that the proportion of coke used is relatively high, and the smelting reduction To solve the problem of high cost, it is proposed to use the residual heat of furnace top gas to preheat saturated steam to generate supersaturated steam, and then inject supersaturated steam from the tuyere of the melting gasifier into the gasifier to replace part of pure oxygen, so that the water gas reaction can be used to regulate The reduction gas composition produced by the melting gasifier can increase the effective reduction components in the reduction gas, thereby increasing the reduction metallization rate of the shaft furnace minerals, reducing the proportion of coke used in smelting reduction production, and making full use of the waste heat of the reduction shaft furnace top gas to reduce melting Reduce production costs and reduce CO2 emissions in the smelting reduction process.

Description

technical field [0001] The invention belongs to the technical field of smelting reduction ironmaking for energy saving and consumption reduction, and in particular relates to a smelting reduction ironmaking method which partially replaces pure oxygen. Background technique [0002] The smelting reduction ironmaking process is the only new industrialized smelting reduction ironmaking process at present. It uses non-coking coal as the main fuel and only uses a small amount of coke to produce high-quality molten iron equivalent to the blast furnace, omitting the indispensable coking of the traditional blast furnace And sintering process, greatly reducing the pollution to the environment, in line with the strategy of sustainable development. [0003] Practice shows that the smelting reduction process still needs to be improved in many aspects, and there is still a lot of room for improvement in technology. Compared with the blast furnace of the same scale, the production cost of ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C21B13/02
Inventor 王玉明胡德生毛晓明钱晖徐万仁
Owner BAOSHAN IRON & STEEL CO LTD
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