Direct Reduction Facility Using Ore Heat to Warm Hydrogen

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current technologies for direct reduction of metal oxide materials into reduced metal materials face challenges in achieving energy efficiency, particularly in using hydrogen as a reducing agent, which requires high reaction temperatures and involves significant energy consumption, often relying on fossil fuels and lacking effective control over production processes.

Innovation Solution

A method and configuration that utilize hydrogen produced by fossil-free and renewable energy sources, where the metal oxide material is pre-heated to a high temperature and combined with a hydrogen-containing reducing agent in a counter-current moving bed reactor, allowing for efficient chemical reaction at reduced temperatures through heat recovery and controlled thermal management.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high reaction temperature is used for direct reduction of metal oxide material by hydrogen, then the chemical reaction efficiency is improved, but the energy consumption increases significantly

Engineering Contradiction:
Improvechemical reaction efficiencyVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The metal oxide material is pre-heated to high temperature (1000-1500°C) in a metal oxide material provider unit before entering the direct reduction facility. This preliminary heating action stores thermal energy in the material, which is then used to maintain reaction temperature during reduction, eliminating the need for continuous external heating and significantly reducing energy consumption while maintaining high reaction efficiency

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system uses the thermal energy stored in the pre-heated metal oxide material to heat the hydrogen-containing reducing agent to the required reaction temperature. The material essentially heats itself and the reducing agent through its own stored thermal energy, creating a self-sustaining thermal process that minimizes external energy input

Inventive Principle:
Principle #25Self-service

2Object-generated harmful factors

If hydrogen is used as reducing agent for direct reduction, then the production becomes CO2-free, but the process requires high energy input and fossil fuel dependency

Engineering Contradiction:
ImproveCO2 emissionsVSAvoidenergy input
Core Design Contradiction:
Object-generated harmful factorsVSUse of energy by moving object

Solution Approach 1:

The metal oxide material is pre-heated to high temperature before reduction, storing thermal energy that eliminates the need for continuous external heating during the CO2-free hydrogen reduction process. This preliminary energy storage action makes the sustainable hydrogen-based reduction process energy-efficient and economically viable

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system changes the thermal energy parameter of the metal oxide material by heating it to 1000-1500°C in the provider unit. This parameter change transforms the material into a thermal energy carrier that can sustain the reduction process without additional fossil fuel input, making the CO2-free process energetically self-sufficient

Inventive Principle:
Principle #35Parameter changes

3Loss of energy

If thermal energy is stored in metal oxide material, then external heating requirements are reduced, but the metal oxide material provider unit complexity increases

Engineering Contradiction:
Improveexternal heating requirementsVSAvoidprovider unit complexity
Core Design Contradiction:
Loss of energyVSDevice complexity

Solution Approach 1:

The metal oxide material provider unit is designed to perform multiple functions: heating the metal oxide material to high temperature, storing the thermal energy in the material, and transporting the pre-heated material to the direct reduction facility. By combining these functions into a single multi-functional unit, the overall system complexity is managed while achieving significant energy efficiency improvements

Inventive Principle:
Principle #6Universality (Multi-functionality)

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 approach achieves a substantially fully metallized reduced metal material with over 90% reduction efficiency, reduces hydrogen accumulation, and enables energy-efficient production with minimal external thermal input, utilizing heat recovery to power high-temperature electrolysis units.

Implementation Method 1

reducing the metal oxide material by using the first thermal energy of the metal oxide material to heat or further heat the introduced hydrogen containing reducing agent toward a required reaction temperature

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

feeding a high-temperature water steam of the high-temperature exit gas to a high-temperature electrolysis unit configured to produce a hydrogen

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 3

providing a chemical reaction between the hydrogen containing reducing agent and the metal oxide material

Methodology Applied
Scientific EffectChemical reaction: Redox Reactions

Data Source

PatentUS20260049370A1A direct reduction facility for reduction of a metal oxide material
Publication Date: 2026.02.19 LOUSSAVAARA KIIRUNAVAORA AB
  • US20260049370A1 patent drawing
  • US20260049370A1 patent drawing
  • US20260049370A1 patent drawing

AI summary

The present invention concerns a metal material production configuration (1) and a method of direct reduction of a metal oxide material (5) holding a first thermal energy into a direct reduced metal material (16) by means of a metal material production configuration (1).The method comprises charging the metal oxide material (5), holding the first thermal energy, into a direct reduction facility (7); introducing a hydrogen, holding a second thermal energy, into the direct reduction facility (7).The invention involves reducing the metal oxide material (5) by using the first thermal energy of the metal oxide material (5) to heat or further heat the introduced hydrogen containing reducing agent (8) toward a required reaction temperature for providing a chemical reaction. A high-temperature exit gas (12) is removed from the direct reduction facility and fed to a high-temperature electrolysis unit (21) configured to produce the hydrogen.