Microwave Hydrogen Plasma Direct Reduced Iron Process

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Solution Overview

Problem

Conventional iron production methods, such as blast furnace processes, result in significant CO2 and CO emissions, as well as energy inefficiency and environmental pollution, due to the use of carbon-based reductants and multiple stages in the production process.

Innovation Solution

A microwave-assisted low-temperature hydrogen plasma process is used to directly reduce iron ore, eliminating the need for carbon-based reductants and reducing the process to a single stage, thereby minimizing CO/CO2 emissions and energy consumption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Object-generated harmful factors

If conventional blast furnace process is used for iron production, then iron can be produced through carbothermic reduction, but significant CO2 and CO emissions are generated causing environmental pollution

Engineering Contradiction:
ImproveCO2 and CO emissionsVSAvoidiron production efficiency
Core Design Contradiction:
Object-generated harmful factorsVSProductivity

Solution Approach 1:

The invention changes the chemical parameters of the reduction process by replacing carbon-based reductants with hydrogen-based reductants. This fundamental parameter change transforms the reduction reaction from carbon-oxide generation to water vapor generation, eliminating CO2 and CO emissions while maintaining efficient iron production through the reaction Fe2O3 + 3H2 → 2Fe + 3H2O

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention substitutes the chemical mechanism of carbothermic reduction with hydrogen reduction. Instead of using carbon (coke) as the reductant which produces CO and CO2, hydrogen gas is used as the reductant which produces only water vapor, thereby replacing the harmful chemical mechanism with an environmentally benign one while maintaining production efficiency

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

2Object-generated harmful factors

If conventional DRI process using carbonaceous materials is used, then iron ore can be reduced, but high carbon content in the product and CO/CO2 emissions are produced

Engineering Contradiction:
ImproveCO/CO2 emissions and carbon content in productVSAvoidproduct purity
Core Design Contradiction:
Object-generated harmful factorsVSManufacturing precision

Solution Approach 1:

The invention extracts and eliminates carbonaceous materials from the reduction process entirely. By removing carbon (coke or coal) as the reductant and replacing it with hydrogen, the source of carbon contamination in the DRI product is eliminated, achieving both zero CO/CO2 emissions and carbon-free or low-carbon DRI product with high purity

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The invention creates a hydrogen-based reducing atmosphere that is inert with respect to carbon contamination. The hydrogen atmosphere serves as a clean environment for reduction that prevents carbon pickup in the iron product, thereby achieving high manufacturing precision and product purity without carbonaceous emissions

Inventive Principle:
Principle #39Inert atmosphere (Inert environment)

3Use of energy by moving object

If multiple stages are used in conventional iron production process, then complete reduction can be achieved, but energy consumption increases

Engineering Contradiction:
Improveenergy consumptionVSAvoidreduction completeness
Core Design Contradiction:
Use of energy by moving objectVSReliability

Solution Approach 1:

The invention merges multiple reduction stages into a single integrated hydrogen reduction process. By using hydrogen as the reductant in a unified process configuration, the need for separate coke-making, sintering, and reduction stages is eliminated, achieving complete reduction in one process while significantly reducing overall energy consumption

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The invention implements continuous hydrogen reduction that maintains consistent reducing conditions throughout the process. The continuous flow of hydrogen through the iron ore ensures sustained and complete reduction without interruption, achieving reliable reduction completeness while avoiding the energy-intensive batch processing of conventional multi-stage methods

Inventive Principle:
Principle #20Continuity of useful action

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This process achieves over 99% reduction of iron oxide with reduced energy consumption and no CO/CO2 emissions, resulting in a more environmentally friendly and energy-efficient production of direct reduced iron (DRI) with lower impurity levels.

Implementation Method 1

microwave assisted low temperature hydrogen plasma

Methodology Applied
Scientific EffectMicrowave plasma: Plasma

Implementation Method 2

heating the holder and sample at temperature ranging between 300-800° C. and pressure ranging between 20-100 torr and at microwave power ranging between 500-1500 W

Methodology Applied
Scientific EffectMicrowave heating: Dielectric Heating

Implementation Method 3

reduction of iron oxide in excess of 99% can be achieved by reducing the ore in hydrogen plasma

Methodology Applied
Scientific EffectChemical reduction: Reduction

Data Source

PatentUS8728195B2Green process for the preparation of direct reduced iron (DRI)
Publication Date: 2014.05.20 COUNCIL OF SCI & IND RES
  • US8728195B2 patent drawing
  • US8728195B2 patent drawing
  • US8728195B2 patent drawing

AI summary

Direct reduced iron (DRI) is obtained from iron ore by reduction using microwave assisted low temperature hydrogen plasma. The process includes steps of: (a) loading iron ore onto a sample holder (b) placing the sample holder inside a chamber followed by evacuating the chamber; (c) introducing hydrogen gas in the chamber at flow rate ranging between 100-500 standard cubic centimeters (sccm) followed by heating the sample holder and the iron ore at a temperature ranging between 300-800° C., a pressure ranging between 20-100 torr and a microwave power ranging between 500-1500 W to obtain direct reduced iron; and (d) cooling the direct reduced iron obtained in step (c) by flowing hydrogen at flow rate of about 300 sccm.