Direct Reduced Iron Gas Treatment via Adsorbent Bed

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Solution Overview

Problem

Existing processes for producing direct reduced iron (DRI) using coke oven gas are limited by high costs associated with cleaning and conditioning due to sulfur compounds and BTX, which contaminate DRI and cause equipment issues, restricting the amount of coke oven gas that can be treated and leading to inefficient steel production.

Innovation Solution

A method and apparatus that utilize a vertical shaft reactor with an adsorbent material outside the reduction zone to adsorb sulfur compounds and BTX from coke oven gas, and a regenerative heater system to crack heavy hydrocarbons, allowing the treated gas to be reused as a reducing agent, thereby minimizing contamination and operational costs.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If coke oven gas is used directly as reducing gas in DRI production, then production costs are reduced and gas utilization is improved, but sulfur compounds and BTX contaminate the DRI product and cause equipment damage

Engineering Contradiction:
Improveproduction costVSAvoidsulfur contamination
Core Design Contradiction:
Ease of manufactureVSObject-affected harmful factors

Solution Approach 1:

The patent applies preliminary action by treating the coke oven gas with an iron ore bed before it enters the reduction zone. The gas passes through a bed of iron ore particles that adsorb sulfur compounds and BTX beforehand, preventing contamination of the DRI product while allowing the gas to be used as reducing agent.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The iron ore bed acts as an intermediary between the coke oven gas and the DRI production process. It selectively removes harmful substances (sulfur compounds and BTX) from the gas stream while allowing the reducing components (CO and H2) to pass through and participate in the reduction reaction.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Manufacturing precision

If extensive cleaning processes are applied to remove sulfur compounds and BTX from coke oven gas, then DRI product quality is improved, but operational costs increase significantly

Engineering Contradiction:
ImproveDRI product qualityVSAvoidoperational cost
Core Design Contradiction:
Manufacturing precisionVSEase of manufacture

Solution Approach 1:

The iron ore bed performs self-service by simultaneously serving dual functions: it acts as both the reducing agent source (providing CO and H2 for reduction) and the purification medium (removing sulfur compounds and BTX). This eliminates the need for separate expensive cleaning equipment and operations.

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The iron ore bed is designed to perform multiple functions within a single unit: it serves as the reducing gas source, the purification medium, and the heat transfer medium. This multi-functionality reduces equipment complexity and operational costs while maintaining high DRI product quality.

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

3Device complexity

If heavy hydrocarbons in coke oven gas are not treated, then equipment complexity is reduced, but hydrocarbon deposits cause pipe plugging and equipment damage

Engineering Contradiction:
Improvegas treatment equipmentVSAvoidequipment reliability
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The patent utilizes parameter changes by heating the coke oven gas to high temperatures (above 700°C) during its passage through the iron ore bed. This temperature change causes heavy hydrocarbons to crack into lighter compounds that do not form deposits, thereby protecting equipment without requiring additional treatment systems.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The heavy hydrocarbons, which would normally cause plugging and equipment damage, are converted into beneficial lighter compounds through thermal cracking. The harmful deposits are transformed into useful lighter hydrocarbons that can participate in the reduction process or be easily removed.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

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 enables the effective and cost-efficient production of high-temperature DRI with reduced sulfur contamination, allowing for increased coke oven gas utilization and improved steel production efficiency by eliminating the need for extensive cleaning processes and reducing equipment damage from hydrocarbon deposits.

Implementation Method 1

caused to flow through a bed of particles of an adsorbent material... whereby sulfur compounds and BTX are adsorbed by said adsorbent material

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 2

whereby sulfur compounds and BTX are adsorbed by said adsorbent material and the heavy hydrocarbons are cracked into lighter compounds by contact with said adsorbent material at high temperature

Methodology Applied
Scientific EffectCracking: Pyrolysis

Implementation Method 3

chemical reduction of iron oxides is carried out by such reducing gas... the reaction of particulate iron ores, mainly iron oxides... with a reducing gas mainly composed of hydrogen and carbon monoxide

Methodology Applied
Scientific EffectChemical reduction: Reduction

Data Source

PatentEP2744922B1Process for producing direct reduced iron (DRI) utilizing gases derived from coal
Publication Date: 2020.07.01 HYL TECH
  • EP2744922B1 patent drawingFigure 1
  • EP2744922B1 patent drawingFigure 2
  • EP2744922B1 patent drawingFigure 3

AI summary

A process for producing direct reduced iron (DRI) from iron ores and reducing the cost and energy requirements of steelmaking, utilizing a gas produced from fossil fuels, containing sulfur compounds and BTX, wherein said gas is heated in a gas heater, wherein heat is transferred from a previously-heated solid material to the gas. The hot gas is caused to flow through a bed of DRI particles, iron oxides or equivalent material, outside of the reduction reactor, where said material adsorbs sulfur compounds and destroying the BTX. The gas resulting from this treatment, free from sulfur compounds and BTX, is combined with a reducing gas stream withdrawn from the reduction reactor after H20 and C02 have at least partially been removed for regenerating its reducing potential with or without undergoing a previous cleaning treatment.