Multi-Tier Transition Zone for High-Carbon DRI Carburization

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current methods for increasing the carbon content of direct reduced iron (DRI) in direct reduction (DR) facilities, such as HDRI and HBI plants, are limited by thermal and equilibrium constraints, typically achieving carbon levels of less than 4.5 wt.%, which is insufficient to meet the demands of steelmakers for higher carbon products that support efficient downstream steelmaking operations.

Innovation Solution

The method involves creating a multi-tiered transition zone within the direct reduction furnace, where carbon monoxide-rich and hydrocarbon-rich gas streams are separately processed and introduced through a circumferential nozzle system, allowing for optimized gas-to-solid contact and temperature-controlled carburization, increasing the carbon content of DRI beyond 4.5 wt.%. This includes separating gas streams into multiple components, blending them to form distinct mixed carburizing gas streams, and introducing these streams at varying temperatures and compositions across multiple tiers of the transition zone.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If conventional single-tier carburization is used in the transition zone, then the process is simple to operate, but the carbon content of DRI is limited to less than 4.5 wt.%

Engineering Contradiction:
Improvecarbon content of DRIVSAvoidgas injection system complexity
Core Design Contradiction:
Quantity of substanceVSDevice complexity

Solution Approach 1:

The transition zone is divided into multiple tiers (typically 3-5 tiers), with each tier having independent gas injection nozzles. This segmentation allows different gas compositions and flow rates to be applied at different heights, optimizing carbon content distribution throughout the DRI burden and achieving carbon levels exceeding 4.5 wt.% while maintaining manageable system complexity through modular design.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention transitions from a single-point or single-level gas injection approach to a multi-dimensional gas distribution system. Gas is injected at multiple vertical levels (tiers) throughout the transition zone, creating a three-dimensional carburization environment that significantly enhances carbon content in the DRI product beyond what conventional single-tier systems can achieve.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Use of energy by moving object

If higher carbon content in DRI is achieved through extended carburization, then energy release during steelmaking is improved, but thermal constraints in the transition zone are exceeded

Engineering Contradiction:
Improveenergy release during steelmakingVSAvoidthermal constraints in transition zone
Core Design Contradiction:
Use of energy by moving objectVSTemperature

Solution Approach 1:

Different gas compositions and injection rates are applied at different tiers of the transition zone. Lower tiers receive gas compositions optimized for carburization, while upper tiers receive compositions that prevent excessive temperature rise. This local quality variation allows high carbon content (>4.5 wt.%) to be achieved without violating overall thermal constraints of the transition zone.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The invention dynamically adjusts multiple parameters including gas composition (CO/H2 ratios), injection pressure, flow rates, and tier-specific distribution patterns. These parameter changes enable precise control of the carburization process, achieving high carbon content in DRI while maintaining thermal balance and preventing overheating in the transition zone.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If multiple mixed carburizing gas streams are introduced through circumferential nozzles, then gas-to-solid contact is optimized for enhanced carburization, but the system complexity and control difficulty increase

Engineering Contradiction:
Improvecarburization efficiencyVSAvoidsystem control difficulty
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

The gas injection system is segmented into multiple independent tiers, each with its own control mechanisms. This segmentation allows operators to control and optimize carburization at each level independently, making the complex multi-stream system manageable through modular operation and simplifying troubleshooting and adjustment procedures.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system incorporates feedback control mechanisms that monitor carbon content, gas flow rates, and temperature at various tiers. This feedback enables automatic adjustment of gas injection parameters to maintain optimal carburization conditions, reducing operational complexity and ensuring consistent high carbon content in the DRI product despite the multi-stream gas injection complexity.

Inventive Principle:
Principle #23Feedback

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 enhances the carburization potential, allowing for the production of DRI with carbon content exceeding 4.5 wt.%, thereby improving the efficiency and economics of the steelmaking process by providing a more significant carbon source for energy release during melting, reducing electrical energy consumption, and maximizing the use of steel scrap in the melter charge material.

Implementation Method 1

The method involves creating a multi-tiered transition zone within the direct reduction furnace, where carbon monoxide-rich and hydrocarbon-rich gas streams are separately processed and introduced through a circumferential nozzle system, allowing for optimized gas-to-solid contact and temperature-controlled carburization

Methodology Applied
Scientific EffectCarburizing: Carburizing

Implementation Method 2

Carbon may be added to DRI within the DR Process through one, or a combination of, carburizing reactions within a countercurrent DR reactor

Methodology Applied
Scientific EffectChemical reactions: Chemical Bonding

Implementation Method 3

allowing for optimized gas-to-solid contact and temperature-controlled carburization

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Data Source

PatentUS12084730B2Methods and systems for increasing the carbon content of direct reduced iron in a reduction furnace
Publication Date: 2024.09.10 MIDREX TECHNOLOGIES INC
  • US12084730B2 patent drawing
  • US12084730B2 patent drawing
  • US12084730B2 patent drawing

AI summary

A method for producing direct reduced iron having increased carbon content, comprises delivering each of the herein-described mixed carburizing gas streams, which are of different composition, to a transition zone of a direct reduction furnace, and exposing partially or completely reduced iron oxide to the mixed carburizing gas streams to increase the carbon content of resulting direct reduced iron to greater than 4.5 wt. %.