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Method for preparing direct reduced iron by bio-oil

A technology of bio-oil and reduced iron, which is applied in chemical instruments and methods, inorganic chemistry, furnace types, etc., can solve the problems of undiscovered bio-oil application, supply, price and regional restrictions, and achieve abundant stocks and be conducive to environmental protection , easy-to-operate effect

Inactive Publication Date: 2009-09-23
UNIV OF SCI & TECH OF CHINA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Visible, at present existing production direct reduction iron technology mainly has two problems: (1) the raw material and fuel that iron oxide is reduced to metal iron in the prior art are coke or natural gas, and this class raw material is non-renewable fossil raw material, Vulnerable to supply, price and regional constraints, and how to reduce harmful gases (CO, NOx, SO 2 ) and greenhouse gas (CO 2 ) emission problems; (2) In the direct reduction iron technology, hydrogen-rich syngas with a high hydrogen-carbon ratio is required as the reducing gas, but whether it is the syngas obtained from gas vaporization or natural gas reforming, CO occupies a large proportion
[0008] So far, no reports have been found on the application of bio-oil to iron reduction technology

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] This example examines the effect of using the method of the present invention to prepare direct reduced iron using bio-oil and hematite powder obtained from rapid pyrolysis of sawdust as raw materials.

[0023]The electrocatalytic steam reforming bio-oil hydrogen production reactor in the prior art (ZL 200710134707.1) is used as the reaction device prepared from bio-oil. The method of preparing reduced synthesis gas from bio-oil: First, the conventional commercial Ni-based catalyst is reduced in a hydrogen atmosphere at 500°C for one hour, and then filled around the built-in electric furnace wire and evenly contacted with the surface of the electric furnace wire, the amount of catalyst is determined by bio-oil per hour The amount of feed is determined. In this embodiment, the amount of catalyst used is 5.5g, and then the power supply of the electric heating belt in the preheating zone is turned on, so that the temperature in the preheating zone is 180-200 ° C; the Ni-Cr ...

Embodiment 2

[0031] This example mainly investigates the effect of using the method of the present invention to prepare direct reduced iron using bio-oil obtained from rapid cracking of rice husk and limonite powder as raw materials.

[0032] In this embodiment, the reaction device and the method for the reduction of synthesis gas from bio-oil and the reduction of iron ore are the same as in Example 1, except that the bio-oil and limonite powder obtained by rapid cracking of rice husk are When making direct reduced iron from raw materials, when the reaction temperature of bio-oil reforming is 548°C, the current is 2.9A, the flow rate of water vapor is 50g / h, the flow rate of bio-oil is 18g / h, and the corresponding molar ratio of water vapor and bio-oil is 7 , the hydrogen production rate and bio-oil conversion rate were 93.5% and 95.1%, respectively, and the cooled mixed gas included hydrogen (69.3vol%), carbon dioxide (24.8vol%), carbon monoxide (5.1vol%) and methane (0.2vol%) , using con...

Embodiment 3

[0036] This example mainly investigates the effect of using the method of the present invention to prepare direct reduced iron by using bio-oil and magnetite powder obtained by rapid pyrolysis of sawdust as raw materials.

[0037] In this example, the reaction device and method for reducing syngas from bio-oil and iron ore reduction are the same as in Example 1. When the bio-oil reforming reaction temperature is 555°C, the current is 3.1A, When the flow rate is 50g / h, the bio-oil flow rate is 18g / h, and the molar ratio of water vapor and bio-oil is 7, the hydrogen production rate and bio-oil conversion rate are 97.2% and 98.9% respectively, and the mixed gas after cooling includes hydrogen (70.8vol%), carbon dioxide (25.5vol%), carbon monoxide (3.5vol%) and methane (0.1vol%), use conventional chemical absorption method (20%NaOH solution) to eliminate carbon dioxide in the mixed gas, and obtain hydrogen containing 93.1vol% and high-grade reducing gas of 4.5vol% carbon monoxide,...

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Abstract

The invention relates to a method for preparing a direct reduced iron by a gas base method, in particular to a technology for preparing the direct reduced iron by taking the bio-oil and iron ore powders as raw materials. The method comprises the following steps of firstly sending the bio-oil and water vapor into a water vapor reforming reactor, converting the carbon-hydrogen-oxygen-contained organic matter in the bio-oil into a mixed gas with principle components of hydrogen and carbon dioxide, obtaining a reduced gas with the hydrogen concentration of more than 90vol% by a tail gas purifying and collecting system, subsequently preheating the reduced gas to the temperature of 100-200 DEG C and sending the preheated gas into a reduction reactor containing the iron ore powders, starting a self-heating system and controlling the temperature in the reduction reactor within 650-900 DEG C and keeping the temperature for 1-2h so that the reduced gas and the ferric oxide in the iron ore generate an oxidation-reduction reaction to obtain the direct reduced iron. The method is characterized in that a coke or a natural gas is not needed and the reproducible bio-oil raw material is used and the method has the advantages of being friendly to environment, simple and quick process, low energy consumption, high metallization rate and high production cost.

Description

technical field [0001] The invention relates to a method for preparing direct reduced iron by using a gas-based method, in particular to a technology for preparing direct reduced iron by using bio-oil and iron ore powder as raw materials. Background technique [0002] At present, there are two main smelting methods for iron and steel production: blast furnace ironmaking technology and direct reduction iron technology using natural gas or coal. Among them, blast furnace ironmaking is the main technical method in steel production at present, accounting for about 90% of the steel production output. It uses high-quality iron ore, coke and solvent for slagging as raw materials. The ironmaking process consists of coking, sintering and blast furnace processes, and the energy consumed accounts for more than 30% of the total energy consumption of steel production. And the traditional steel industry is a serious source of pollution. Another method is the direct reduction iron technol...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C21B13/00C21B13/10C01B3/38
CPCY02P10/143
Inventor 李全新巩飞艳袁丽霞鸟本善章
Owner UNIV OF SCI & TECH OF CHINA
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