Rapid-Heating Coking Coal for Blast Furnace Coke Strength

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Solution Overview

Problem

The challenge is to enhance the operational efficiency and productivity of blast furnaces while increasing the use of non- or slightly-coking coals while maintaining or exceeding conventional coke strength, as existing methods are inefficient and require multiple steps.

Innovation Solution

A method involving rapid-heating of blended coals in a fluidized-bed to a temperature range between 300° C. and the softening point, followed by classification and forming of fine-size coal, which is then blended with coarse-size coal and carbonized, eliminating the need for pre-classification of non- or slightly-coking coals from strongly-coking coals.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Strength

If conventional methods are used to maintain coke strength with depleting high-quality coal resources, then coke strength is maintained, but productivity and operational efficiency deteriorate due to inability to use low-quality coals

Engineering Contradiction:
Improvecoke strengthVSAvoidoperational efficiency
Core Design Contradiction:
StrengthVSProductivity

Solution Approach 1:

The invention changes the thermal parameters by applying rapid heating (heating rate of 100-1000°C/sec) to non- or slightly-coking coals, transforming their physical and chemical properties to achieve caking behavior similar to high-quality coals, thereby enabling their use in metallurgical coke-making while maintaining coke strength

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention performs preliminary classification of coals into size fractions before heating, and conducts rapid heating and agglomeration operations before carbonization, preparing the low-quality coals in advance to acquire caking properties needed for strong coke production

Inventive Principle:
Principle #10Preliminary action

2Stability of the object's composition

If multiple classification and treatment steps are applied to improve caking properties of low-quality coals, then caking properties are enhanced, but device complexity and operational complexity increase

Engineering Contradiction:
Improvecaking propertiesVSAvoidprocess steps
Core Design Contradiction:
Stability of the object's compositionVSDevice complexity

Solution Approach 1:

The invention merges the classification and heating operations into an integrated process where coals are classified by size and then rapidly heated in sequence, combining multiple functions into a streamlined workflow that reduces the number of separate equipment units and operational steps required

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The invention segments the coal charge by particle size (fine coal not more than 0.3 mm and coarse coal over 0.3 mm) to apply appropriate heating and treatment conditions to each fraction, enabling effective improvement of caking properties through targeted processing

Inventive Principle:
Principle #1Segmentation

3Stability of the object's composition

If rapid-heating is applied to improve caking properties of non- or slightly-coking coals, then caking properties are enhanced, but energy consumption increases due to high heating rates required

Engineering Contradiction:
Improvecaking propertiesVSAvoidenergy consumption
Core Design Contradiction:
Stability of the object's compositionVSUse of energy by moving object

Solution Approach 1:

The invention applies rapid heating specifically to the fine coal fraction (not more than 0.3 mm) which requires the most intensive treatment to develop caking properties, while the coarse coal fraction is preheated at a moderate rate, optimizing energy distribution across different size fractions based on their specific needs

Inventive Principle:
Principle #16Partial or excessive 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 method allows for the production of high-strength coke using large quantities of non- or slightly-coking coals, enhancing caking properties without classification, thereby increasing operational efficiency and reducing production costs.

Implementation Method 1

rapid-heating said coking coal in a fluidized-bed to a temperature range between not lower than 300° C. and not higher than the temperature at which the coking coal begins to soften

Methodology Applied
Scientific EffectFluidization: Fluidisation

Implementation Method 2

rapid-heating of blended coals in a fluidized-bed to a temperature range between 300° C. and the softening point

Methodology Applied
Scientific EffectConvection heating: Convection

Implementation Method 3

rapid-heating said fine-size coal and coarse-size coal individually in a pneumatic preheater to a temperature range between not lower than 300° C. and not higher than the temperature at which the coking coal begins to soften

Methodology Applied
Scientific EffectPneumatic transport:

Implementation Method 4

rapid-heating said fine-size coal and coarse-size coal individually in a pneumatic preheater at a rate of 103 to 105° C./min.

Methodology Applied
Scientific EffectConvection heating: Convection

Implementation Method 5

classifying the rapid-heated coking coal to fine-size coal and coarse-size coal

Methodology Applied
Scientific EffectCyclone separation: Cyclone Separation

Implementation Method 6

forming said fine-size coal

Methodology Applied
Scientific EffectAgglomeration:

Data Source

PatentUS7645362B2Method for pretreating and improving coking coal quality for blast furnace coke
Publication Date: 2010.01.12 KOBE STEEL LTD
  • US7645362B2 patent drawing
  • US7645362B2 patent drawing
  • US7645362B2 patent drawing

AI summary

Methods for pretreating and improving coking coal quality for producing blast-furnace coke by: (a) rapid-heating the coal charge in a fluidized-bed to a temperature range between not lower than 300° C. and not higher than the temperature at which the coal charge begins to soften, at a rate of 30 to 103 ° C./min., (b) classifying the rapid-heated coal charge to fine- and coarse-size coal, and then (c-1) briquetting the fine-size coal or (c-2) rapid-heating the fine- and coarse-size coal individually in a pneumatic preheater to a temperature range between not lower than 300° C. and not higher than the temperature at which the coal charge begins to soften, at a rate of 103 to 105 ° C./min., and (d) forming the fine-size coal.