Hydrothermal Sludge Dewatering via Piston Press and Cooling

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Solution Overview

Problem

Current methods for ultra-dehydrating sewage sludge face high energy consumption, odor management issues, and automation challenges, particularly in achieving and storing sludge with at least 50% dryness without self-ignition and efficient thermal recovery.

Innovation Solution

Combining hydrothermal carbonization with a piston press, where products are pressurized and thermally conditioned in a closed reactor, followed by dehydration using a piston press, with odor control measures to prevent atmospheric diffusion and automate the process.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If thermal drying is used to achieve ultra-dehydration of sludge, then dryness greater than 50% is obtained, but energy consumption increases to 900-1100 kWh/TEE

Engineering Contradiction:
Improvedryness contentVSAvoidenergy consumption
Core Design Contradiction:
Quantity of substanceVSUse of energy by moving object

Solution Approach 1:

The dehydration process is divided into two distinct stages: a first dehydration stage using a filter press to achieve initial dewatering (4-25% dryness), and a second ultra-dehydration stage using thermal drying to achieve final dryness (>50%). This segmentation allows each stage to operate optimally, reducing overall energy consumption compared to direct thermal drying.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The filter press performs preliminary dehydration before thermal drying, removing a significant portion of water content upfront. This preliminary action reduces the water load on the thermal dryer, thereby reducing the energy required for the subsequent ultra-dehydration stage.

Inventive Principle:
Principle #10Preliminary action

2Extent of automation

If filter press is used for dewatering, then automation is difficult, but if thermal drying is used, then automation is easier

Engineering Contradiction:
Improveautomation capabilityVSAvoidfilter cake removal complexity
Core Design Contradiction:
Extent of automationVSDevice complexity

Solution Approach 1:

The filter press and thermal drying unit are merged into an integrated system where the filter press handles initial dewatering and the thermal dryer completes ultra-dehydration. This combination allows the automated thermal drying unit to handle the complex ultra-dehydration task while the filter press handles preliminary processing, achieving both automation and effective dewatering.

Inventive Principle:
Principle #5Merging (Combining)

3Reliability

If sludge is stored with high dryness content, then self-ignition risk decreases, but storage complexity increases

Engineering Contradiction:
Improveself-ignition resistanceVSAvoidstorage management complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The dryness content parameter of sludge is changed from low (conventional) to high (>50%, preferably 65% or more) through the two-stage dehydration process. This parameter change fundamentally alters the storage characteristics, eliminating self-ignition risks and enabling long-term stable storage without complex safety management systems.

Inventive Principle:
Principle #35Parameter changes

4Quantity of substance

If direct thermal drying is used, then ultra-dehydration is achieved, but odor release into atmosphere occurs

Engineering Contradiction:
Improvedryness contentVSAvoidodor emission
Core Design Contradiction:
Quantity of substanceVSObject-generated harmful factors

Solution Approach 1:

The dehydration process is segmented into a filter press stage and a thermal drying stage, with each stage operating in a controlled manner. The thermal drying unit, being a closed system, handles the ultra-dehydration while containing odors, and the filter press handles preliminary dewatering separately, reducing overall odor emission into the atmosphere.

Inventive Principle:
Principle #1Segmentation

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

Significantly reduces energy consumption, effectively manages odors, and enables automated production and storage of ultra-dehydrated sludge with improved dryness and thermal recovery, while preventing self-ignition and odor spread.

Implementation Method 1

dehydration of the products by piston press

Methodology Applied
Scientific EffectMechanical pressure: Compression

Implementation Method 2

dehydration of the products by piston press, until a dryness greater than 50% is obtained

Methodology Applied
Scientific EffectFiltration: Filter (physical)

Implementation Method 3

the temperature of the product upstream of dehydration by piston press being regulated by cooling between 40 and 90°C

Methodology Applied
Scientific EffectCooling: Cooling

Implementation Method 4

hydrothermal carbonization type treatment, including pressurization and thermal conditioning for residence in a closed reactor

Methodology Applied
Scientific EffectThermal conditioning: Heating

Implementation Method 5

hydrothermal carbonization of dehydrated sludge

Methodology Applied
Scientific EffectHydrothermal carbonization: Pyrolysis

Implementation Method 6

followed by decompression, then dehydration of the products by piston press

Methodology Applied
Scientific EffectDecompression: Depressurisation

Data Source

PatentEP2991934B1Method for ultra dewatering viscous or pasty biomass forming products and installation for carrying out the method
Publication Date: 2019.07.10 TERRANOVA ENERGY
  • EP2991934B1 patent drawingFigure 1
  • EP2991934B1 patent drawingFigure 2
  • EP2991934B1 patent drawingFigure 3~4

AI summary

The invention relates to a method for ultra-dehydrating thickened or pasty biomass products, in particular sludge from wastewater treatment plants, according to which the products, in particular products having a dryness of 4 % to 25 %, are subjected to the following steps: hydrothermal carbonisation treatment, including pressurization (1, 2) and thermal conditioning (30) for a duration in a closed reactor (4); followed by dehydration of the products by a ram press (12), obtaining a dryness of more than 50 %; the temperature of the product upstream from the ram press dehydration being regulated by cooling between 40 °C and 90 °C, advantageously to around 70 °C, in order to optimise the filterability in the piston press; the steps of the method being performed in a confined space making it possible to prevent the release of smells into the atmosphere.