Scraped-Surface Salt Separator for Supercritical Salt Clogging

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Solution Overview

Problem

Existing salt separators in thermochemical conversion processes, particularly for supercritical water gasification, face inefficiencies in separating type II salts, which can clog equipment and require high thermal or mechanical energy inputs, and existing antifouling solutions are not effective for these small particles.

Innovation Solution

A salt separator with a scraper plate and internal filters, capable of retaining microparticles and nanoparticles, is used to separate and regenerate salts under controlled temperature conditions, allowing continuous operation and efficient salt removal.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional salt separators are used in supercritical water gasification, then salt separation can be achieved, but type II salts (microparticles and nanoparticles) clog the equipment and require high thermal or mechanical energy inputs

Engineering Contradiction:
Improvesalt separation effectivenessVSAvoidequipment clogging by type II salts
Core Design Contradiction:
ReliabilityVSObject-affected harmful factors

Solution Approach 1:

The invention extracts and removes type II salts (microparticles and nanoparticles) from the supercritical water stream using a dedicated filtration system with filters specifically designed to capture these fine particles, preventing them from clogging downstream equipment

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The invention introduces an intermediary cooling zone that transforms the supercritical water into subcritical or liquid phase, causing type II salts to precipitate and become amenable to filtration, thereby mediating between the supercritical reaction environment and the salt removal mechanism

Inventive Principle:
Principle #24Intermediary (Mediator)

2Reliability

If conventional salt separators are used, then salt separation can be achieved, but excessively high inputs of thermal or mechanical energy are required

Engineering Contradiction:
Improvesalt separation effectivenessVSAvoidthermal and mechanical energy input
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The invention changes the temperature and pressure parameters of the supercritical water to subcritical or liquid phase conditions in a controlled cooling zone, inducing salt precipitation without requiring high energy inputs for mechanical separation or thermal processing

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention utilizes the phase transition of water from supercritical to subcritical or liquid state to drive salt precipitation and separation, leveraging natural thermodynamic changes rather than consuming additional thermal or mechanical energy

Inventive Principle:
Principle #36Phase transitions

3Reliability

If conventional salt separators are used, then salt separation can be achieved, but salts are combined with a significant portion of organic material

Engineering Contradiction:
Improvesalt separation effectivenessVSAvoidorganic material contamination with salts
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

The invention creates a localized filtration environment with specifically designed filters that target type II salts while allowing organic materials to pass through, achieving selective separation based on particle size and properties

Inventive Principle:
Principle #3Local quality

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

The solution effectively prevents clogging and enables continuous operation by retaining and regenerating salts, improving the efficiency and longevity of thermochemical conversion facilities.

Implementation Method 1

a scraper plate (13) which is slidingly mounted in the tube (10) and in the inner chamber (C) of the enclosure along a path which generates scraping friction directly with the internal wall of the tube (10) and/or with any solid material deposit, including the precipitated salts

Methodology Applied
Scientific EffectFriction: Friction

Implementation Method 2

at least one salt filter housed and fastened in the inner chamber, the salt filter being adapted to retain the salts within it, once they have been precipitated in the inner chamber, including those in the form of microparticles and nanoparticles

Methodology Applied
Scientific EffectFiltration: Filter (physical)

Implementation Method 3

an outer one (21) of which, which is thermally insulating, incorporates heating elements (22) which thus heat the chamber (C) and the injection tube (10)

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 4

supercritical water gasification of biomass... water at temperatures greater than 374° C. under a pressure greater than 22.1 MPa

Methodology Applied
Scientific EffectSupercritical fluid: Supercritical Fluid

Implementation Method 5

the precipitation occurs virtually instantaneously as soon as the temperature reached leads to a decrease in the solubility of the salts

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Data Source

PatentUS20250387729A1Scraped-surface salt separator with a scraper plate which slides into a precipated-salt resolubilization zone and associated biomass gasification facility
Publication Date: 2025.12.25 COMMISSARIAT A LENERGIE ATOMIQUE ET AUX ENERGIES ALTERNATIVES
  • US20250387729A1 patent drawing
  • US20250387729A1 patent drawing
  • US20250387729A1 patent drawing

AI summary

A separator for salts contained in a solution which is brought under supercritical conditions, with at least one salt filter which can retain therein salts initially contained in the solution and which are precipitated, including those in the form of micro- or nanoparticles. The operation of the salt separator makes it possible, if necessary, to heat the solution for conversion to a temperature ensuring the precipitation of the salts and their retention within suitable filters and then to separate the solution for conversion into a salt-depleted stream which is discharged from the separator and directed to a conversion reactor, in particular a gasification reactor, and, if appropriate, into a stream loaded with salts to be extracted in the form of a brin.