Two-Stage Sludge Drying Using Evaporate Heat Recovery

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Solution Overview

Problem

Existing sludge drying technologies face inefficiencies due to limited waste heat recovery and challenges posed by the glue zone, which affects heat transfer and mechanical wear, particularly in friction dryers operated by large electrical motors.

Innovation Solution

A two-stage sludge drying system where evaporated water from a first dryer is used to indirectly heat a second dryer, with controlled recycling of partially dry sludge to maintain optimal dryness levels and utilize waste heat efficiently, while operating the dryers at different pressures and temperatures to manage the glue zone and enhance heat transfer.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by moving object

If waste heat recovery is improved by using evaporated water from the first dryer to heat the second dryer, then energy efficiency is improved, but system complexity increases

Engineering Contradiction:
Improveenergy efficiencyVSAvoidsystem complexity
Core Design Contradiction:
Use of energy by moving objectVSDevice complexity

Solution Approach 1:

The evaporated water from the first dryer serves as an intermediary heat transfer medium. It is condensed in a heat exchanger to release latent heat, which then heats the second dryer indirectly. This intermediary approach enables efficient waste heat recovery while isolating the two drying processes, managing system complexity through modular heat exchange components.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The system recovers waste heat from the evaporated water that would otherwise be discarded from the first dryer. By condensing this evaporated water and utilizing its latent heat to pre-heat or heat the second dryer, the system transforms a waste stream into a valuable energy resource, significantly improving overall energy efficiency.

Inventive Principle:
Principle #34Discarding and recovering

2Productivity

If friction dryers are used to dry sludge, then drying capability is improved, but mechanical wear and electrical energy consumption increase

Engineering Contradiction:
Improvedrying capabilityVSAvoidmechanical wear
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The drying process is segmented into two distinct stages: a first dryer handling initial drying and a second dryer handling final drying. This segmentation allows each dryer to operate under optimized conditions, reducing the mechanical stress and wear on any single unit while maintaining high overall drying capability.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system replaces direct mechanical friction drying with indirect thermal drying using heat exchangers. Instead of relying on mechanical friction between moving parts and sludge, the invention uses thermal energy transfer through condensing evaporated water, eliminating mechanical wear while preserving drying effectiveness.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Productivity

If the glue zone is encountered during sludge drying, then heat transfer efficiency decreases, but drying continues

Engineering Contradiction:
Improvedrying continuationVSAvoidheat transfer efficiency
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The first dryer performs preliminary drying of the sludge before it enters the second dryer. By removing a significant portion of moisture in the first stage, the sludge enters the second dryer at an optimal moisture content that avoids or minimizes the formation of the glue zone, thereby maintaining heat transfer efficiency in the second dryer.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system changes operating parameters between the two dryers, including temperature, pressure, and residence time. By optimizing these parameters in each stage, the system prevents the sludge from entering the glue zone condition where heat transfer efficiency deteriorates, ensuring continuous effective drying throughout the process.

Inventive Principle:
Principle #35Parameter changes

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 significant energy savings and reduces mechanical wear by optimizing heat recovery and avoiding the glue zone, resulting in a more efficient and durable sludge drying process.

Implementation Method 1

Water is evaporated from the wet sludge stream in the first dryer to generate a partially dry sludge stream

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 2

The evaporated water in the first dryer is used to indirectly heat the sludge in the second dryer

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 3

The use of the heat in the evaporated water generated in the first dryer for indirect heating in the second dryer provides an energy efficient sludge drying system

Methodology Applied
Scientific EffectWaste heat recovery: Heat Exchanger

Data Source

PatentEP4107127B1Sludge drying method
Publication Date: 2026.02.18 FJELL TECH GRP AS
  • EP4107127B1 patent drawingFigure 1

AI summary

Disclosed herein is a sludge drying system comprising: a system input for receiving a wet sludge stream, wherein the wet sludge stream comprises water and solid material; a first dryer arranged to receive, at an input of the first dryer, the wet sludge stream and to heat the wet sludge stream such that at least part of the water in the wet sludge stream is evaporated to thereby generate evaporate and a partially dry sludge stream, wherein the first dryer is an indirectly heated rotating disc dryer that comprises a first output for outputting evaporate and a second output for outputting the partially dry sludge stream; a second dryer that is an indirectly heated rotating disc dryer and is arranged to receive, at a first input of the second dryer, a stream that is dependent on the partially dry sludge stream output from the first dryer and to receive, at a second input of the second dryer, the evaporate from the first dryer, wherein the second dryer is arranged to use to the received evaporate to indirectly heat the received stream at the first input to thereby generate and output a substantially dry sludge stream; and a system output for outputting at least part of the substantially dry sludge stream from the system.