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Gas base and coal base combined shaft furnace direct reduction process

A combined, shaft furnace technology, applied in shaft furnaces, furnaces, furnace types, etc., can solve problems such as restricting wide application, production cost and engineering investment are difficult to be competitive, and achieve lower production costs, strong resource adaptability, The effect of process simplification

Inactive Publication Date: 2019-11-15
WUHAN COSRED SCI & TECH LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this technology requires an additional set of gas generators and related ancillary treatment facilities, which makes the production cost and engineering investment of this technology difficult to be competitive. These deficiencies will seriously restrict the direct reduction of the existing gas-based shaft furnace Wide application of technology

Method used

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  • Gas base and coal base combined shaft furnace direct reduction process
  • Gas base and coal base combined shaft furnace direct reduction process

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Such as figure 1 As shown, lignite is used as the main raw material for the production of reducing gas, and pellets, lignite and limestone of suitable particle size are mixed with 1000kg of pellets to add 500-2500kg of lignite and 30-250kg of limestone to form a mixture 101, from The top of the shaft furnace reactor 100 is loaded into the furnace, and a part of lignite powder 102 is sprayed into the upper area 104 of the shaft furnace reactor from the lignite lance 103. Position; the temperature in the upper area 104 and the middle area 106 of the shaft furnace reactor is maintained at a suitable temperature between 800-1350 °C, the reducing gas and material flow in the furnace are all running downward, and the temperature in the lower area 107 of the shaft furnace reactor is 500~750℃. The pyrolysis of lignite in the furnace, the gasification reaction of carbon, and the reduction reaction of pellets are completed in the middle area 106 of the shaft furnace reactor.

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Embodiment 2

[0031] Such as figure 2 As shown, lignite is used as the main raw material for the production of reducing gas, and pellets, lignite and limestone of suitable particle size are mixed with 1000kg of pellets to add 500-2500kg of lignite and 30-250kg of limestone to form a mixture 101, from The top of the shaft furnace reactor 100 is loaded into the furnace; the temperature of the upper area 104 and the middle area 106 of the shaft furnace reactor is maintained at a suitable temperature between 800 and 1350 ° C, and the reducing gas and material flow in the furnace are all running downwards. The temperature in the lower zone 107 of the shaft furnace reactor is 500-750°C. The pyrolysis of lignite in the furnace, the gasification reaction of carbon, and the reduction reaction of pellets are completed in the middle area 106 of the shaft furnace reactor.

[0032] The reducing gas 201 is discharged from the exhaust port at the lower part of the shaft furnace reactor, and the exhaust ...

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Abstract

The invention relates to a gas base and coal base combined shaft furnace direct reduction process. Solid carbon materials and iron-contained minerals are mixed to load in a shaft furnace reactor, andthe pyrolytic gasification reaction of the solid carbon materials and the reduction reaction of the iron-contained minerals are finished in the shaft furnace reactor; furnace internal reduction gas and furnace burdens are operated down; the downward operation speed of the furnace internal reduction gas is higher than the downward operation speed of materials; products are discharged from a discharge port at the bottom of the shaft furnace reactor after reduction, and the furnace internal reduction gas is exhausted from an exhaust port at the lower part of the shaft furnace reactor; after exhausting of the reduction gas, components thereof are adjusted according to the demands, and the reduction gas is reheated to reach a temperature of 800-1350 DEG C as heat carrying gas; and the heat carrying gas is fed in the furnace from an intake port at the upper part of the shaft furnace reactor to provide needed heat for the pyrolytic gasification reaction of the solid carbon materials and the reduction reaction of the iron-contained minerals in the furnace. The pyrolytic gasification reaction of the solid carbon materials and the reduction reaction of the iron-contained minerals are integrated to finish in one set of shaft furnace devices, so that the energy utilization efficiency is improved, and the production cost and the engineering investment are reduced.

Description

technical field [0001] The invention belongs to the field of non-blast furnace ironmaking, and in particular relates to a gas-based and coal-based shaft furnace direct reduction process. Background technique [0002] The non-blast furnace ironmaking process includes two categories: direct reduction process and smelting reduction process. The direct reduction ironmaking process can be divided into two categories according to the different reducing agents used: gas-based direct reduction method using gas reducing agent and solid reduction method The coal-based direct reduction method of the agent. [0003] Typical representatives of the current gas-based direct reduction process are the Midrex shaft furnace method and the Energiron / HYL shaft furnace method. These two shaft furnace methods are currently the most widely used gas-based direct reduction processes, and their typical characteristics are: after preparing qualified high-temperature reducing gas through a series of de...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C21B13/02
CPCC21B13/0066C21B13/0073C21B13/02
Inventor 付邦豪周强李建涛唐恩汪朋陈泉锋
Owner WUHAN COSRED SCI & TECH LTD