Two-Stage Agglomeration for Non-Caking Coal Briquettes
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Solution Overview
Problem
The challenge lies in effectively utilizing non-classic feedstocks such as brown coal and weakly caking hard coal in coking processes, particularly in vertical chamber furnaces, where achieving sufficient compressive strength and maintaining water content within narrow tolerance ranges is crucial to prevent briquette breakdown and ensure efficient coking.
Innovation Solution
A two-stage agglomeration process involving a perforated disk roller mill for initial pelletization and a molding channel stamp press for briquetting, with controlled temperature and moisture management, to produce high-strength briquettes with a cylindrical geometry, ensuring optimal packing and coking performance.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Adaptability or versatility
If non-conventional feedstocks (lignite, low-caking hard coal) are used for coking, then the range of usable feedstocks is expanded and mining costs are reduced, but the compressive strength of briquettes is insufficient and they disintegrate during coking
Solution Approach 1:
The coking process is segmented into two distinct stages: a first coking stage at lower temperature (400-700°C) to form green briquettes with initial structural integrity, and a second coking stage at higher temperature (700-1100°C) to achieve final coke quality. This segmentation allows non-conventional feedstocks to be processed progressively, building strength in stages rather than requiring immediate high-temperature resistance
Solution Approach 2:
Green briquettes are formed and partially coked before being subjected to final high-temperature coking. The preliminary low-temperature coking stage pre-cooks the feedstock and establishes basic structural framework, so that when the briquettes enter the second coking stage, they already have improved integrity and can withstand the thermal and mechanical stresses of high-temperature processing
2Ease of operation
If water content in feedstock is increased to improve handling and prevent premature drying, then briquette flexibility is improved, but compressive strength decreases and briquettes become prone to breakdown
Solution Approach 1:
The feedstock is pre-treated in a pugmill mixer where water and binders are uniformly distributed throughout the material before briquetting. This preliminary water distribution ensures that moisture is evenly incorporated, allowing the briquettes to maintain flexibility during handling while developing sufficient strength through the controlled coking process
Solution Approach 2:
Binders are introduced as intermediary substances that mediate between water and coal particles. The binders absorb water and create binding bridges between particles, allowing the system to maintain both flexibility (through water) and strength (through binder-mediated particle bonding) simultaneously during the briquetting and initial drying phases
3Device complexity
If conventional single-stage coking is used for non-caking coals, then the process is simple, but the coke quality is unsatisfactory and briquettes disintegrate in vertical chamber furnaces
Solution Approach 1:
The coking operation is divided into two sequential stages with distinct temperature ranges and duration parameters. The first stage (400-700°C, 0.5-2 hours) focuses on moisture removal and initial carbonization, while the second stage (700-1100°C, 1-4 hours) completes the coking process. This segmentation provides reliable briquette integrity by progressively transforming the material rather than subjecting it to abrupt high-temperature stress
Solution Approach 2:
The coking process utilizes systematic parameter changes across two stages: temperature increases from 400-700°C to 700-1100°C, and residence time is allocated as 0.5-2 hours in the first stage and 1-4 hours in the second stage. These controlled parameter transitions ensure that non-caking coals undergo gradual structural transformation, maintaining reliability while achieving the necessary coke quality
4Strength
If high compressive force is applied during briquetting to increase strength, then briquette density improves, but the feedstock requires higher moisture content which complicates drying and coking
Solution Approach 1:
Binders serve as intermediaries that enable effective particle bonding at lower compression forces. The binders create adhesive bridges between coal particles, allowing the formation of strong green briquettes without requiring excessive mechanical pressure, thereby avoiding the need to add large amounts of water that would complicate subsequent drying and coking operations
Solution Approach 2:
The reliance on mechanical compression to achieve particle bonding is partially replaced by chemical bonding mechanisms provided by binders. Instead of depending solely on high mechanical pressure to force particles together, the binders provide chemical adhesion that maintains briquette integrity at lower compression levels, simplifying the moisture management requirements
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 production of high-quality, pressure-resistant briquettes that maintain strength and shape during coking, enhancing operational efficiency and coke quality, even with inferior coal qualities, and expanding the range of usable feedstocks.
Implementation Method 1
a first agglomeration stage with a perforated disc roller mill (79), in which the feedstock (1) is compacted into pellets (1.1)
Implementation Method 2
a first agglomeration stage with a perforated disc roller mill (79)
Implementation Method 3
a second agglomeration stage with a pressing device (73), designed as a molding channel stamp press
Implementation Method 4
with a correspondingly designed pressing channel (73.1) and pressing ram (75)
Implementation Method 5
at least one briquette dryer (15) configured for tempering briquettes (5) produced from the feedstock (1)
Implementation Method 6
the briquette dryer has a heating device and a briquette reservoir heatable thereby
Implementation Method 7
conveyed through a shaft-like coking chamber due to gravitational forces from top to bottom and is continuously heated
Implementation Method 8
the required thermal energy is stored in at least two, preferably at least three horizontal heating channels arranged laterally on one side of the respective furnace chamber
Data Source
Figure 1~5
Figure 2
Figure 3
AI summary
The invention relates to a tool device (70) for compacting solid, in particular carbonaceous input material into briquettes, with an apparatus for compressing the input material; wherein the tool device comprises a first agglomeration stage (70.1) with a perforated-disc roller mill (79), wherein the compressing apparatus has a shaping channel punch press (73) having at least one pressing punch (75) and a corresponding pressing channel (73.1) and is connected downstream of the perforated-disc roller mill as a second agglomeration stage (70.2), wherein the perforated-disc roller mill (79) comprises a die (79.1) having a plurality of pressing apertures (79.2), each of which has a diameter of up to 6 mm or between 1 and 6 mm, in particular less than 3 mm. The invention further relates to a method for compacting solid, in particular carbonaceous input material as well as the use of individual plant components in a two-stage agglomeration.